Corrosion inhibition with alkoxy aromatic imidazolines

ABSTRACT

An aminoalkyl imidazolines of the formula: 
     
       
         
         
             
             
         
       
     
     having p-octyloxy-, p-dodecyloxy-, or p-octadecyloxy-phenyl pendants as hydrophobes, for use to mitigate mild steel corrosion. An electron-rich -aromatic ring, in conjugation with an amidine motif, imparts increasing corrosion inhibition efficiencies with an increasing hydrophobe chain length. X-ray photoelectron spectroscopy confirms the formation of an aminoalkyl imidazoline film on a metal surface prior to reaching a critical molar concentration.

BACKGROUND OF THE INVENTION

The present disclosure is directed to the synthesis and preparation of imidazoline compounds and their use as corrosion inhibitors in metallic flow lines.

DESCRIPTION OF THE RELATED ART

The “background” description provided herein is for the purpose of generally presenting the context of the disclosure. Work of the presently named inventors, to the extent it is described in this background section, as well as aspects of the description which may not otherwise qualify as prior art at the time of filing, are neither expressly or impliedly admitted as prior art against the present invention.

The oil and gas industries experience huge economic losses as a result of the damage corrosion inflicts on pipes, at d other plaits systems. [S. Nesic, Key issues related to modelling of internal corrosion of oil and gas pipelines-A review, Corros. Sci. 49 (2007) 4308-4338. Incorporated herein by reference in its entirety.] Corrosion can be defined as the gradual degredation of a material by a chemical reaction of said material with its environment. It is noticeably problematic for materials that comprise a metal, as it can compromise, or even destroy, many of the metal's useful properties such as strength and appearance. In particular, corrosion has a detrimental effect on a metallic surface, such as the surfaces of steel sheeting and pipes, when these surfaces are placed in contact with petroleum and/or petroleum products.

Petroleum, herein defined as crude oil, has many constituents. The natural constituents of crude petroleum are known as petroleum products. These include, but are not limited to, gasoline, jet fuel, diesel fuel, heating oil, and other heavy fractions which result in the production of asphalt, tar, and paraffin wax. Surprisingly, although known to be vulnerable to corrosion, metals such as steel are commonly used throughout the petroleum industry to form the majority of pipelines transporting petroleum and petroleum products.

Steel itself can be classified by elasticity parameters and carbon content. For example, mild steel is an alloy comprised of metals and non-metals, along with a high amount of carbon. The oil and gas industries rely heavily on this type of steel to form pipes and pipelines in order to transport crude and refined oil. As such, these industries are increasingly concerned with the need to minimize corrosion in light of high economic replacement costs and ever-growing environmental safety concerns.

Environments that are warm, halic, and acidic are generally more corosive to metals than those that are cooler, non-halic, and alkaline. Metal surfaces, in particular, experience electrochemical oxidation, or corrosion, when exposed to acidic (low pH) surroundings. This type of corrosion is particularly aggravated when metal parts and surfaces are in continuous contact with acidic aqueous environments, such as those occuring within pipelines carrying petroleum and/or petroleum products which have been obtained through an enhanced oil recovery process.

Enhanced oil recovery is defined as the implementation of various techniques for increasing the amount of crude oil that can be extracted from an oil field. Several techniques exist; however, gas injection, or miscible flooding, is presently the most commonly used approach in enhanced oil recovery. The term miscible flooding refers specifically to an injection processes that introduce miscible gases into a reservoir resulting in a displacement process. This displacement process maintains the reservoir pressure and moreover improves oil displacement, thus increasing oil recovery.

Although carious gases can be used for miscible flooding, hydrogen sulfide and carbon dioxide are the favored choices due to their low cost and viscosity reducing properties. Consequently, the corrosive environment encountered in oil wells is either anaerobic or aerobic, and contains ‘sour’ (containing hydrogen sulfide) or sweet (containing carbon dioxide) corrosive components.

“Sweet corrosion” can be further defined as the corrosion of carbon and low-alloy steel by carbonic acid and its derivatives. It is therefore evident that the high levels of CO₂ and/or H₂S introduced during miscible flooding result in the formation of acidic aqueous conditions. Notably, contact between the metal surfaces of a pipeline system and the aqueous acidic petroleum products of an enhanced oil recovery process, can occur during all phases of hydrocarbon recovery and refining. Alloy technology has recently provided materials that can withstand the incidental contact of steel with corrosive components such as NaCl, CO₂ and/or H₂S, but the corrosion problem is intensified when there is no choice but to continuously contact steel with these components, as in the case of hydrocarbon exploration, recovery, and refining.

In addition to the level of acidity or alkalinity within a transport pipeline system, the level of corrosion is influenced by several other factors. These include, but are not limited to, the metallurgy and age of the pipeline, the temperature and pressure at which the pipeline is operated, the flow patterns, water accumulation, and turbulent intensity of the flow, the fluid chemistry concerning CO₂, H₂S, O₂, and NaCl content, the inherent corrosiveness of the fluid flowing through the pipeline, and the presence, or lack of, an inhibitor, and the ability of an existent inhibitor to maintain adhesion to the surface of the pipe in the transport pipeline system.

Metallurgy refers in part to the chemical composition and surface morphology of the pipeline. If mild steel is exposed to an aerated neutral aqueous solution, such as a dilute solution of sodium chloride in water, corrosive attack will begin at any defects found in a previously formed oxide film on said mild steel. These defects may be present as a result of mechanical damage such as scratches, or may be due to natural discontinuities in the film, i.e. inclusions, grain boundaries or dislocation networks at the surface of the steel.

At each defect the steel is exposed to the solution (electrolyte), an anodic reaction will occur, resulting in the formation of iron ions and free electrons. These electrons are then conducted through the oxide film to take part in a cathodic reaction at the surface of the film. This reaction requires the presence of dissolved oxygen in the electrolyte which furthers a response favoring the formation of hydroxyl ions. Thus, the surface morphology plays a distinct role in initiating the anodic reaction of a corrosive process.

Several methods exist to limit both the occurance and progression of corrosion. They include the selection of a corrosion resistant material for the pipeline, such as stainless steel, plastics, and special alloys. Inert barriers, such as coatings and linings that are placed between the pipe wall and the flowing fluid also limit corrosion. These barriers are often applied in conjunction with cathodic protection systems. Additional measures include the use of chemical corrosion inhibitiors. Chemical corrosion inhibitors are injected into the pipeline to reduce the pH, act as a barrier, and react with possible oxidizing agents. As such, chemical corrosion inhibitors have been the subject of considerable research.

In general, the choice of a corrosion inhibitor varies according to the nature of the corrosive environment. For example, in order to transport petroleum products, the oil industry uses large-diameter flow lines in oil field applications. Pipelines in these situations can transport large volumes of produced oil and water at extremely high flow rates from the field to a processing station at rates ranging up to 50 m/sec. The ability of an added corrosion inhibitor to completely cover the interior of the line, and subsequently, the ability of the added corrosion inhibitors to maintain adhesion to the interior of the line, depends on both the chemical adhesive properties of the inhibitor and the shear stress conditions which exist inside the line. Understandably, corrosion inhibitors with good adhesive qualities under high shear stress conditions are therefore necessitated.

Due to the eco-toxicity of many corrosion inhibitors, it is essential to use those inhibitors which are active at a concentration that does not harm the environment. Gas and oil production processes often take place offshore or along a coastline. If a corrosion inhibitor enters the sea or a stretch of fresh water, it can potentially harm microorganisms, and other aquatic life, and thus detrimentally effect the environment. Recent attempts have therefore been made to identify successful corrosion inhibitors which are less toxic to the environment than previously known inhibitors.

Many relevant inhibitor compositions are based upon amines, amides, or imidazolines; often in combination with other types of inhibitors. Imidazoline corrosion inhibitors exhibit both high efficiency and low toxicity, and furthermore, are advantageously synthesized from environmentally friendly raw materials.

In addition to their use in the petroleum industry, imidazolines can also limit corrosion in a solvent-based post combustion capture system, such as those which release large sources of CO₂ emissions. These include, but are not limited to, such systems as coal-fired power plants, refineries, cement manufacturing and the like, where corrosion can affect every part of the process equipment. Imidazolines can also be employed as inhibitors of corrosion formed on metallic surfaces resulting from exposure to a steam condensate. Examples include those generated from steam generating systems such as steam boilers, cooling water systems, and heat transfer water systems.

Currently, imidazolines are the most extensively used inhibitors to combat CO₂ corrosion. (Y. Jovancicevic, S. Ramachandran, P. Prince, Inhibition of carbon dioxide corrosion of mild steel by imidazolines and their precursors, Corrosion 55 (1999) 449-455. X. Liu, S. Chen, H. Ma, G. Liu, L. Shen, Protection of iron corrosion by stearic acid and stearic imidazoline self-assembled monolayers, Appl. Surf. Sci. 253 (2006) 814-820. X. Liu, P. C. Okafor, Y. G. Zheng, The inhibition of CO₂ corrosion of N80 mild steel in single liquid phase and liquid/particle two-phase flow by aminoethyl imidazoline derivatives, Corros. Sci. 51 (2009) 744-751. P. C. Okafor, X. Liu, Y. G. Zheng, Corrosion inhibition of mild steel by ethylamino imidazoline derivative in CO₂-saturated solution, Corros. Sci. 51 (2009) 761-768. F. Farelas, A. Ramirez, Carbon dioxide corrosion inhibition of carbon steels through bis-imidazoline and imidazoline compounds studied by EIS, Int. J. Electrochem. Sci. 5 (2010) 797-814. M. W. S. Jawich, G. A. Oweimreen, S. A. Ali, Heptadecyl-tailed mono- and bis-imidazolines: A study of the newly synthesized compounds on the inhibition of mild steel corrosion in a carbon dioxide saturated saline medium, Corros. Sci. 65 (2012) 104-112. Incorporated herein by reference in their entirety.]

Imidazolines are defined as a class of heterocycles formally derived from imidazoles by the addition of H₂ across one of two double bonds. Three isomers are known: 2-imidazoline, 3-imidazoline, and 4-imidazoline. The 2- and 3-imidazolines contain an imine center and the 4-imidazoline contains an alkene group.

The chemical architecture of an imidazoline inhibitor frequently includes the following: a five-membered heterocycle containing an electron-rich hydrophilic amidine (N═C—N) group, a pendent side chain containing one or more electron-donor hydrophilic functional group(s) (R₁) and a hydrophobic alkyl chain (R₂) attached to the carbon atom of the amidine group, respectively (1).

The ring-nitrogens in imidazolines of structure (2) are weakly nucleophilic but are strong bases in compounds such as 1,8-diazabicyclo[5.4.0]undec-7-ene (DBU) (pK_(b) 1.1) and 1,5-Diazabicyclo[4.3.0]non-5-ene (DBN) (pK_(b) 0.5). [P. A. Koutentis, M. Koyioni, S. S. Michaelidou, Synthesis of [(4-Chloro-5H-1,2,3-dithiazol-5-ylidene)amino]azines, Molecules 16 (2011) 8992-9002. Incorporated herein by reference in its entirety.]

In the presence of CO₂, the bases are reported to form bicarbonate salts (3) in aqueous media: [W. Qiao, Z. Zheng, Q. Shi, Synthesis and properties of a series of CO₂ switchable surfactants with imidazoline group, J. Surfact. Deterg. 15 (2012) 533-539 D. J. Heldebrant, P. G. Jessop, C. A. Thomas, C. A. Eckert, C. L. Liotta. The Reaction of 1,8 Diazabicyclo[5.4.0]undec-7-ene (DBU) with carbon dioxide, J. Org. Chem. 70 (2005), 5335-5338. Incorporated herein by reference in their entirety.] Imidazolines, upon partial hydrolysis in aqueous solution, are converted into amides (4). [W. Qiao, Z. Zheng, Q. Shi, Synthesis and properties of a series of CO₂ switchable surfactants with imidazoline group, J. Surfact. Deterg. 15 (2012) 533-539 Incorporated herein by reference in its entirety].

The reaction of an amine having a pK_(b) of ≈4 in aqueous CO₂ solution is complex; [N. Ramachandran, A. Aboudheir, R. Idem, P. Tontiwachwuthikul, Kinetics of the absorption of CO₂ into mixed aqueous loaded solutions of monoethanolamine and methyldiethanolamine, Ind. Eng. Chem. Res. 45 (2006) 2608-2616. P. N. Sutar, A. Jha, P. D. Vaidya, E. Y. Kenig, Secondary amines for CO₂ capture: A kinetic investigation using N-ethylmonoethanolamine, Chem. Eng. J. 207-208 (2012) 718-724. Incorporated herein by reference in their entirety.]in addition to the formation of carbamate salts 5a & 5b, and bicarbonate salt 6, several ionic and neutral species such as HCO₃ ⁻, CO₃ ²⁻, OH⁻, H₃O⁺, CO₂ and H₂O are also known to coexist. Due to the large number of compounds (1-6) and additional ionic species, it is difficult to ascertain with certainty which of the compounds (1-6) and/or ionic species are involved in imparting inhibitory properties, and thus, the mechanism by which an imidazoline imparts corrosion inhibition is complex and poorly understood.

Crude oil itself is corrosive to mild steel; CO₂/H₂O, injected into oil wells to increase production, [X. Jiang, Y. G. Zheng, D. R. Qu, W. Ke. Effect of calcium ions on pitting corrosion and inhibition performance in CO₂ corrosion of N80 steel, Corros. Sci. 48 (2006) 3091-3108 Incorporated herein in its entirety.] has been found to be more aggressive than hydrochloric acid at the same pH. [G. Zhang, C. Chen, M. Lu, C. Chai, Y. Wu, Evaluation of inhibition efficiency of an imidazoline derivative in CO₂-containing aqueous solution, Mater. Chem. Phys. 105 (2007) 331-340. U. Lotz, L. Van Bodegom, C. Ouwehand, The effect of type of oil or gas condensate on carbonic acid corrosion, Corrosion 47 (1991) 635-644, Incorporated herein by reference in their entirety.] It is not the dry CO₂, but rather its aqueous solution, which imparts corrosiveness. The enhanced corrosion is attributed to the increased cathodic reduction of the species H⁺, HCO₃ ⁻ as well as H₂CO₃, all of which are involved in mobile equilibria in an aqueous solution of CO₂. [F. F. Eliyan, A. Alfantazi, On the theory of CO₂ corrosion reactions—Investigating their interrelation with the corrosion products and API-X100 steel microstructure, Corros. Sci. 85 (2014) 380-393. Q. Y. Liu, L. J. Mao, S. W. Zhou, Effects of chloride content on CO₂ corrosion of carbon steel in simulated oil and gas well environments, Corros. Sci. 84 (2014) 165-171. Incorporated herein by reference in their entirety.]

The main reactions on the surface of the metal are represented by Eqs. (1)-(5) [F. F. Eliyan, A. Alfantazi, On the theory of CO₂ corrosion reactions—Investigating their interrelation with the corrosion products and API-X100 steel microstructure, Corros. Sci. 85 (2014) 380-393. Q. Y. Liu, L. J. Mao, S. W. Zhou, Effects of chloride content on CO₂ corrosion of carbon steel in simulated oil and gas well environments, Corros. Sci. 84 (2014) 165-171. K. Chokshi, W. Sun, S. Nesic, Iron carbonate scale growth and the effect of inhibition in CO₂ corrosion of mild steel, NACE International Corrosion Conference & Expo, Paper #05285, 2005 Incorporated herein by reference in their entirety]:

Fe(s)+2H₂CO₃(aq)

Fe(HCO₃)₂(aq)+H₂(g)  (1)

Fe(s)+2H⁺(aq)

Fe²⁺(aq)+H₂(g)  (2)

Fe²⁺(aq)+2H₂O

Fe(OH)₂(s)+2H⁺(aq)  (3)

Fe(OH)₂(s)

FeO(s)+H₂O  (4)

Fe(HCO₃)₂(aq)

FeCO₃(s)+H₂CO₃(aq)  (5)

A coating of iron (II) carbonate on the metal surface is beneficial as it can minimize the rate of the corrosion process. [J. Han, D. Young, H. Colijn, A. Tripathi, S. Nesic, Chemistry and structure of the passive film on mild Steel in CO₂ corrosion environments, Ind. Eng. Chem. Res. 48 (2009) 6296-6302. Incorporated herein by reference in its entirety.] The solubility of iron (II) carbonate increases with an increase in temperature, while it dissolves at a lower pH values. Corrosion inhibitors, especially organic compounds containing electron-rich hetero-atoms, and alkyl chain hydrophobes, [F. Farelas, M. Galicia, B. Brown, N. Nesic, H. Castaneda, Evolution of dissolution processes at the interface of carbon steel corroding in a CO₂ environment studied by EIS, Corros. Sci. 52 (2010) 509-517. Incorporated herein by reference in its entirety.] are used to minimize mild steel corrosion. The inhibitor molecules may undergo physi- and/or chemisorption and form a hydrophobic barrier film to shield the hydrophobes from the hostile corrosive media. [F. Bentiss, M. Triasnel, H. Vezin, M. Lagrenee, Linear resistance model of the inhibition mechanism of steel in HCl by triazole and oxadiazole derivatives: Structure-activity correlations, Corros. Sci. 45 (2003) 371-380. Incorporated herein by reference in its entirety.]

The effects of hydrophilic and hydrophobic substituents of imidazolines on their inhibition efficiency (IE) have been discussed in some detail. [V. Jovancicevic, S. Ramachandran, P. Prince, Inhibition of carbon dioxide corrosion of mild steel by imidazolines and their precursors, Corrosion 55 (1999) 449-455, A. Edwards, C. Osborne, S. Webster, D. Klenerman, M. Joseph, P. Ostovar, M. Doyle, Mechanistic studies of the corrosion inhibitor oleic imidazoline, Corros. Sci. 36 (1994) 315-325. S. Ramachandran, B. L. Tsai, M. Blanco, H. Chen, Y. Tang, W. A. Goddard, III, The SAM mechanism for corrosion inhibition of iron by imidazolines, Langmuir 12 (1996) 6419-6428. X. Zhang, F. Wang, Y. He, Y. Du, Study of the inhibition mechanism of imidazoline amide on CO₂ corrosion of Armco iron, Corros. Sci. 43 (2001) 1417-1431. D. Wang, S. Yong, M. Wang, H. Xiao, Z. Chen, Theoretical and experimental studies of structure and inhibition efficiency of imidazoline derivatives, Corros. Sci. 41 (1999) 1911-1919. Incorporated herein by reference in their entirety.] Some suggest a greater role played by the N pendent [A. J. Szyprowski, Hydrogen sulphide corrosion of steel—Mechanism of action of imidazoline inhibitors, Proceeding of the Eighth European Symposium on Corrosion Inhibitor (8SEIC) Univ. Ferrara, (1995) 1229-1238. Incorporated herein by reference in its entirety.], while others indicate the opposite [A. Edwards, C. Osborne, S. Webster, D. Klenerman, M. Joseph, P. Ostovar, M. Doyle, Mechanistic studies of the corrosion inhibitor oleic imidazoline, Corros. Sci. 36 (1994) 315-325. Incorporated herein by reference in its entirety.] There are also contradictory reports on the importance of the length of the hydrophobic alkyl chain on corrosion inhibition. [V. Jovancicevic, S. Ramachandran, P. Prince, Inhibition of carbon dioxide corrosion of mild steel by imidazolines and their precursors, Corrosion 55 (1999) 449-455. S. Ramachandran, B. L. Tsai, M. Blanco, H. Chen, Y. Tang, W. A. Goddard, III, The SAM mechanism for corrosion inhibition of iron by imidazolines, Langmuir 12 (1996) 6419-6428. Incorporated herein by reference in their entirety.] The inhibition efficacy of the imidazolines is attributed to their ability to form a chemisorbed film on the iron surface. [V. Jovancicevic, S. Ramachandran, P. Prince, Inhibition of carbon dioxide corrosion of mild steel by imidazolines and their precursors, Corrosion 55 (1999) 449-45522. Edwards, C. Osborne, S. Webster, D. Klenerman, M. Joseph, P. Ostovar, M. Doyle, Mechanistic studies of the corrosion inhibitor oleic imidazoline, Corros. Sci. 36 (1994) 315-325. Incorporated herein by reference in their entirety.] The poorly understood and highly complex mechanism of CO₂ corrosion has, in the past, impeded the design of new molecules as inhibitors. [A. Edwards, C. Osborne, S. Webster, D. Klenerman , M. Joseph, P. Ostovar, M. Doyle, Mechanistic studies of the corrosion inhibitor oleic imidazoline, Corros. Sci. 36 (1994) 315-325. G. McIntire, J. Lippert, J. Yudelson, The effect of dissolved CO₂ and O₂ on the corrosion of iron, Corrosion 46 (1990) 91-95. Incorporated herein by reference in their entirety.]

Accordingly, corrosion inhibitors suitable for the protection of metals exposed to environments containing carbon dioxide, and exhibiting superior adhesive qualities under high shear stress conditions, are needed.

The above-described methods and compounds illustrate conventional techniques for preventing and inhibiting corrosion, and include the preparation and use of imidazolines as corrosion inhibitors. Accordingly, one objective of the present disclosure is to provide a series of imidazoline compounds and a method for their preparation.

BRIEF SUMMARY OF THE INVENTION

The present disclosure relates to a series of aminoalkyl imidazolines, and formulations thereof, for use as corrosion inhibitors.

In a first embodiment, the present invention is directed to an aminoalkyl imidazoline represented by the following structural formula (I)

wherein m is an integer of 1 to 10; R is a C₁-C₆ alkylene; R₁ is selected from the group consisting of aromatic groups of formula (II)

wherein X is a heteroatom independently selected from the group consisting of oxygen and sulfur;

R′₁ thru R′₅ are each independently selected from the group consisting of hydrogen, C₁-C₃₀ alkyl, alkenyl, aryl, alkylaryl, arylalkyl, aminoalkyl, and aminoaryl;

further wherein R′₅ is preferably a C₅-C₂₀ alkyl, most preferably a C₈-C₁₈ alkyl;

R₂ and R₃ are each independently selected from the group consisting of hydrogen, hydroxyl, halogen, C₁-C₃₀ alkyl, alkenyl, aryl, alkylaryl, arylalkyl, aminoalkyl, and aminoaryl, (CH₂)₂COOH, CH₂CH(CH₃)COOH and imidazoline.

In a preferred embodiment, the aminoalkyl imidazoline of formula (I) comprises a 2-imidazoline ring substituted with an ethanamine group at a 5-N position of the 2-imidazoline ring, and a p-octyloxy phenyl group at a 1-C position of the 2-imidazoline ring; so as to provide a 1-(2-aminoethyl)-2-(4-octyloxypheny)-2-imidazoline.

In a preferred embodiment, the aminoalkyl imidazoline of formula (I) comprises a 2-imidazoline ring substituted with an ethanamine group at a 5-N position of the 2-imidazoline ring, and a p-dodecyloxy phenyl group at a 1-C position of the 2-imidazoline ring; so as to provide a 1-(2-aminoethyl)-2-(4-dodecyloxyphenyl)-2-imidazoline.

In a preferred embodiment, the aminoalkyl imidazoline of formula (I) comprises a 2-imidazoline ring substituted with an ethanamine group at a 5-N position of the 2-imidazoline ring, and a p-octadecyloxy phenyl group at the 1-C position of the 2-imidazoline ring; so as to provide a 1-(2-aminoethyl)-2-(4-octadecyloxyphenyl)-2-imidazoline.

In a preferred embodiment, the aminoalkyl imidazoline of formula (I) comprises a 2-imidazoline ring substituted with a N¹-(2-aminoethyl)-N²-ethylethane-1,2-diamine group at a 5-N position of the 2-imidazoline ring, and a p-octyloxy phenyl group at a 1-C position of the 2-imidazoline ring; so as to provide a 1-[2-{2-(2-aminoethylamino)ethylamino}ethyl]-2-(4-octyloxyphenyl)-2-imidazoline.

In a preferred embodiment, the aminoalkyl imidazoline of formula (I) comprises a 2-imidazoline ring substituted with a N¹-(2-aminoethyl)-N²ethylethane-1,2-diamine group at a 5-N position of the 2-imidazoline ring, and a p-dodecyloxy phenyl group at a 1-C position of the 2-imidazoline ring; so as to provide a 1-[2-{2-(2-aminoethylamino)ethylamino}ethyl]-2-(4-dodecyloxyphenyl)-2-imidazoline.

In a preferred embodiment, the aminoalkyl imidazoline of formula (I) comprises a 2-imidazoline ring substituted with a N¹-(2-aminoethyl)-N²-ethylethane-1,2-diamine group at a 5-N position of the 2-imidazoline ring, and a p-octadecyloxy phenyl group at the 1-C position; so as to provide a 1-[2-{2-(2-aminoethylamino)ethylamino}ethyl]-2-(4-octadecyloxyphenyl)-2-imidazoline.

In a further embodiment, the aminoalkyl imidazolines of formula (I) are used in a process for preventing or reducing corrosion of a metallic flow line.

In a further embodiment, the aminoalkyl imidazolines of formula (I) are prepared by reacting a nitrile with a polyethylene polyamine in the presence of an acid catalyst at a temperature ranging from 140° C.-150° C.

In a preferred embodiment, the aminoalkyl imidazoline of formula (I) is prepared by reacting diethylene triamine (DETA) with 4-(octyloxy) cyclohexanecarbonitrile in the presence of a cysteine HCl catalyst at a temperature of 145° C. to yield 1-(2-aminoethyl)-2-(4-octyloxyphenyl)-2-imidazoline.

In a preferred embodiment, the aminoalkyl imidazoline of formula (I) is prepared by reacting diethylene triamine (DETA) with 4-(dodecyloxy) cyclohexanecarbonitrile in the presence of a cysteine HCl catalyst at a temperature of 145° C. to yield 1-(2-aminoethyl)-2-(4-dodecyloxyphenyl)-2-imidazoline.

In a preferred embodiment, the aminoalkyl imidazoline of formula (I) is prepared by reacting diethylene triamine (DETA) 4-(octadecyloxy) cyclohexanecarbonitrile in the presence of a cysteine HCl catalyst at a temperature of 145° C. to yield 1-(2-aminoethyl)-2-(4-octadecyloxyphenyl)-2-imidazoline.

In a preferred embodiment, the aminoalkyl imidazoline of formula (I) is prepared by reacting tetraethylene pentamine (TEPA) with 4-(octyloxy) cyclohexanecarbonitrile in the presence of a cysteine HCl catalyst at a temperature of 145° C. to yield 1-[2-{2-(2-aminoethylamino)ethylamino}ethyl]-2-(4-octyloxyphenyl)-2-imidazoline.

In a preferred embodiment, the aminoalkyl imidazoline of formula (I) is prepared by reacting tetraethylene (TEPA) with 4-(dodecyloxy) cyclohexanecarbonitrile in the presence of a cysteine HCl catalyst at a temperature of 145° C. to yield 1-[2-{2-(2-aminoethylamino)ethylamino}ethyl]-2-(4-dodecyloxyphenyl)-2-imidazoline.

In a preferred embodiment, the aminoalkyl imidazoline of formula (I) is prepared by reacting tetraethylene pentamine (TEPA) with 4-(octadecyloxy) cyclohexanecarbonitrile in the presence of a cysteine HCl catalyst at a temperature of 145° C. to yield 1-[2-{2-(2-aminoethylamino)ethylamino}ethyl]-2-(4-octadecyloxyphenyl)-2-imidazoline.

In a further embodiment, an aminoalkyl imidazoline of formula (I) is present in a composition further comprising one or more additives selected from the group comprising surfactants, intensifiers, solvents, oil-wetting components, dispersants biocides and/or scale inhibitors.

In another embodiment, the present disclosure includes a method for preventing or reducing corrosion comprising adding to a process stream an effective corrosion inhibiting amount of one or more aminoalkyl imidazolines of formula (I)

wherein m is an integer of 1 to 10; R is a C₁-C₆alkylene; R₁ is selected from the group consisting of aromatic hydrocarbons of formula (II)

wherein X is a heteroatom independently selected from the group consisting of oxygen and sulfur;

R′₁ thru R′₅ are each independently selected from the group consisting of hydrogen, C₁-C₃₀ alkyl, alkenyl, aryl, alkylaryl, arylalkyl, aminoalkyl, and aminoaryl;

further wherein R′₅ is preferably a C₅-C₂₀ alkyl, most preferably a C₈-C₁₈ alkyl;

R₂ and R₃ are each independently selected from the group consisting of hydrogen, hydroxyl, halogen, C₁-C₃₀ alkyl, alkenyl, aryl, alkylaryl, arylalkyl, aminoalkyl, and aminoaryl, (CH₂)₂COOH, CH₂CH(CH₃)COOH and imidazoline.

In a further embodiment, the aminoalkyl imidazoline is added to the process stream at a dosage of 0.1 ppm to 10,000 ppm by weight of the aminoalkyl imidazoline.

In a further embodiment, the aminoalkyl imidazoline is added to the process stream at a dosage of 1.0 ppm to 1000 ppm by weight of the aminoalkyl imidazoline.

In a most preferred embodiment, the aminoalkyl imidazoline is added to the process stream at a dosage of 1.0 ppm to 500 ppm by weight of the aminoalkyl imidazoline.

In a further embodiment, the process stream comprises at least one constituent selected from the group consisting of water, petroleum and/or petroleum products, and at least one constituent selected from the group consisting of carbon dioxide (CO₂), hydrogen sulfide (H₂S), oxygen (O₂), and NaCl.

In a further embodiment the aminoalkyl imidazoline is added continuously to the process stream.

In a further embodiment the aminoalkyl imidazoline is added intermittently to the process stream.

In a further embodiment the aminoalkyl imidazoline suppresses an anodic reaction of a metal corrosive process.

In a preferred embodiment, the metal is a mild steel.

In another aspect, the disclosure relates to a method of inhibiting corrosion of a metal surface undergoing continuous and/or intermittent contact with a process stream wherein said process stream comprises water and/or hydrocarbons, comprising;

applying at least one aminoalkyl imidazoline compound of the first embodiment to a surface of a metal, wherein said applying comprises a spraying or a dipping of a metal surface and/or an adding to said process stream contacting said metal surface, of said imidazoline so as to cover and maintain an effective application on at least one surface of a metal in contact with said process stream;

wherein said effective concentration comprises an amount of 0.1 ppm to 10,000 ppm by weight of the aminoalkyl imidazoline; preferably 1.0 ppm to 1,000 ppm by weight of, most preferably 1.0 ppm to 500 ppm parts by weight of the aminoalkyl imidazoline;

wherein the aminoalkyl imidazoline is added to a metallic flow line continuously or intermittently so as to maintain an effective corrosion inhibiting dose;

wherein said aminoalkyl imidazoline mainly suppresses an anodic reaction of a metal corrosive process.

In a further embodiment, the metallic flow line comprises mild steel.

In a further embodiment, a flow rate of the process stream through the metallic flow line ranges from 0-50 m/sec.

In a further embodiment a flow rate of the process stream through the metallic flow line ranges from 10-30 m/sec.

The foregoing paragraphs have been provided by way of general introduction, and are not intended to limit the scope of the following claims. The described embodiments, together with further advantages, will be best understood by reference to the following detailed description taken in conjunction with the accompanying drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

A more complete appreciation of the disclosure and many of the attendant advantages thereof will be readily obtained as the same becomes better understood by reference to the following detailed description when considered in connection with the accompanying drawings, wherein:

FIG. 1 shows an ¹H NMR spectra of the imidazolines (IXa) in CDCl₃.

FIG. 2 shows an ¹H NMR spectra of the imidazolines (VIIIa) in CDCl₂.

FIG. 3 shows a ¹³C NMR spectra of the imidazoline (IXc) in the δ 40-55 ppm range in CDCl₃.

FIG. 4 shows a ¹³C NMR spectra of the imidazolines (VIIIc) in the δ 40-55 ppm range in CDCl₃.

FIG. 5A shows a potentiodynamic polarization curve(s) at 40° C. for mild steel in CO₂ saturated 0.5 M NaCl containing various concentrations of VIIIc, FIG. 5B shows a potentiodynamic polarization curve(s) at 40° C. for mild steel in CO₂ saturated 0.5 M NaCl containing various concentrations of IXc, FIG. 5C shows a potentiodynamic polarization curve(s) at 40° C. for mild steel in CO₂ saturated 0.5 NaCl containing 50 ppm of VIII a, b, c and FIG. 5D shows a potentiodynamic polarization curve(s) at 40° C. for mild steel in CO₂ saturated 0.5 M NaCl containing 50 ppm of IX a,b,c.

FIG. 6A shows a Langmuir adsorption isotherm of VIII a, b, c, FIG. 6B shows a Langmuir adsorption isotherm of IX a, b, c at 40° C., FIG. 6C shows a Langmuir adsorption isotherm of VIIIc and FIG. 6D shows a Langmuir adsorption isotherm of IXc at various temperatures in CO₂ saturated 0.5 NaCl solution.

FIG. 7 shows a variation of ΔG°_(ads) versus T on mild steel in CO₂ saturated 0.5 M NaCl containing VIIIc and IXc.

FIG. 8A shows a “Surface Tension versus Concentration” of imidazoline VIII a, b, c. and VIIIa-CO₂, FIG. 8B shows a “Surface Tension versus Concentration” of imidazoline IX a,b,c in 0.5 M NaCl solution, FIG. 8C shows inhibition efficiency versus concentration of imidazolines VIIIa,b,c in CO₂ saturated 0.5 M NaCl solution at 40° C. and FIG. 8D shows inhibition efficiency versus concentration of imidazolines IX a,b,c in CO₂ saturated 0.5 M NaCl solution at 40° C.

FIG. 9A shows an XPS spectrum of Fe after immersing in CO₂ saturated 0.5 M NaCl at 40° C. for 6 h in the presence of VIIIc (100 ppm). FIG. 9B shows an XPS deconvoluted profile of C 1 s after immersing in CO₂ saturated 0.5 M NaCl at 40° C. for 6 in the presence VIIIc (100 ppm), FIG. 9C shows an XPS deconvoluted profile of N 1 s after immersing in CO₂ saturated 0.5 M NaCl at 40° C. for 6 h in the presence of VIIIc (100 ppm), FIG. 9D shows an XPS spectrum of Fe in the presence of IXc, FIG. 9E shows an XPS deconvoluted profile of C 1 s in the presence of IXc, and FIG. 9F shows an XPS deconvoluted profile of N 1 s in the presence of IXc.

FIG. 10A shows an XPS deconvoluted profile of O 1 s in the presence of 100 ppm of IXa, FIG. 10B shows an XPS deconvoluted profile of Fe 2 p in the presence of 100 ppm of IXb, and FIG. 10C shows an XPS deconvoluted profile of N 1 s in the presence VIIIb (100 ppm) after immersing Fe in CO₂ saturated 0.5 M NaCl at 40° C. for 6 h.

FIG. 11A shows a ¹³C NMR spectra of VIIIa (in CDCl₃, using TMS as internal standard), FIG. 11B shows a ¹³C NMR spectra of VIIIa-CO₂ (in D₂O using dioxin as an external standard) and FIG. 11C shows a ¹³C NMR spectra of VIIIa-H⁺(HCO₃ ⁻)CO₂ (in D₂O using dioxin as an external standard).

DETAILED DESCRIPTION OF THE EMBODIMENTS

Referring now to the drawings, wherein like reference numerals designate identical or corresponding parts throughout the several views.

Aminoalkyl imidazolines of this disclosure effectively prevent and/or inhibit the formation of corrosion on metal materials and equipment, such as metallic flow lines, used in a process for producing and/or transporting petroleum and petroleum products. Furthermore, the aminoalkyl imidazolines of this disclosure effectively prevent and/or inhibit the formation of corrosion on metal materials and equipment, such as metallic pipelines, in a process comprising producing and/or transport a process stream. The aminoalkyl imidazolines of this disclosure also mitigate the corrosion of metal materials and equipment employed in related processes wherein steam or other corrosive fluids and/or gases are contained in a process stream.

Methods of reducing corrosion comprise adding to a process stream an effective corrosion inhibiting amount of one or more of the aminoalkyl imidazolines as disclosed herein. Said processes include, but are not limited to, processes involving cleaning and hydrocarbon recovery operations. With respect to oil and gas production, it is well known that during the production life of an oil or gas well, the production zone, including tubular goods, downhole tools and other equipment within the well, may be exposed to corrosive conditions. With respect to the process stream, a stream comprising a fluid such as, but not limited to, water, petroleum, petroleum products, and hydrocarbons wherein said fluid may be found in a liquid or vapor phase in said stream, forms an aqueous and/or petroleum phase. Said stream may further comprise carbon dioxide (CO₂), hydrogen sulfide (H₂S,) and/or NaCl, and, in combination with the aqueous and/or a petroleum phase, form the process stream.

As an amount of the aminoalkyl imidazoline compounds disclosed herein can be used to inhibit corrosion of metals in acid and/or alkaline environments, the amount that is defined for use is dependent on the particular environment that it is intended for. A suitable amount, or proportion, or dosage, can be determined empirically by taking into account parameters such as, but not limited to, the nature of the process stream and the proportion of corrosive species therein, the nature of the metal being protected, the flow rate of the process stream, the temperature and pressure of said process stream, and the amount of time said metal is contacted by the process stream.

Herein, ppm is defined as the amount of inhibitor as found in a process stream by weight of the inhibitor. The aminoalkyl imidazoline inhibitor is preferably added to the process stream at a dosage of 0.1 ppm to 10,000 ppm by weight of the aminoalkyl imidazoline, more preferably at a dosage of 1.0 to 1000 ppm by weight of the aminoalkyl imidazoline, and most preferably at a dosage of 10 to 500 ppm by weight of the aminoalkyl imidazoline. Furthermore, the corrosion inhibitors as individually disclosed herein may be used singularly (neat), or in combination—with or without blending together—to enhance a corrosion inhibition performance.

For handling, injection and distribution, any number or combination of other components may be added to the herein disclosed aminoalkyl imidazolines to formulate them into a liquid form, or otherwise formulate them in order to enhance their performance. The components comprise surfactants, intensifiers, solvents, oil-wetting components and/or dispersants. Suitable components, which are also compatible with the process, include, but are not limited to, water, fatty acid esters, ethylated alcohols, sodium sulfonate, isopropanol, aliphatic distillates, aromatics, heptane, di-isobutyl ketone, methyl isobutyl ketone, glycols, high boiling oils, xylene, toluene, and naphtha.

The imidazoline inhibitor may also be used in combination with other materials commonly employed in corrosion inhibiting compositions such as, but not limited to, scale inhibitors and biocides.

The aminoalkyl imidazoline, and any additives such as the above mentioned solvents and/or dispersants, can be injected directly into the process stream by, but not limited to, (a) injection at different locations into the process stream, (b) as separate formulations injected at the same location, or (c) injection together as part of a single combined formulation. It is also within the scope of this disclosure to have several injection sites located at various distance intervals along a pipeline containing a process stream so as to present said aminoalkyl imidazolines to a process stream environment in which they are most suited to inhibit corrosion. In a preferred embodiment, the aminoalkyl imidazolines are added continuously. In another preferred embodiment, the aminoalkyl imidazolines are added intermittently.

In a further embodiment, the adding to a process stream of an effective corrosion inhibitor(s) comprises introducing, adding or injecting at least one imidazoline of this disclosure through a member or conduit positioned within an initial proximal portion of a pipeline or well carrying a process stream. The process stream may contain compounds such as, but not limited to, water, petroleum, petroleum products, hydrocarbons, and acidic species such as CO₂ and/or H₂S, and NaCl. The methods herein also encompass a plurality of injection sites located at various intervals along said pipeline, or well, carrying said process stream, for additional injection of said imidazoline compounds tailored to treat corrosion at a specific site of the pipeline or well.

Furthermore, inhibition of corrosive process of a metal, such as mild steel, can occur by mitigating the corrosion found at a metal surface to contact with a process stream. Said process stream as previously defined, includes, but is not limited to, water, petroleum, petroleum products, hydrocarbons, and acidic species such as CO₂ and/or H₂S, and NaCl. Said inhibition of the corrosion comprises administering an effective concentration of an aminoalkyl imidazoline of this disclosure. Administering comprises applying at least one aminoalkyl imidazoline compound of the disclosure to a surface of a metal, wherein said applying comprises a spraying or a dipping of a metal surface and/or an adding to said process stream contacting said metal surface, of said imidazoline so as to cover and maintain an effective application on at least one surface of a metal in contact with said process stream.

The aminoalkyl imidazolines of this invention mainly suppresses an anodic reaction of the metal corrosive process, and maintain adhesion to said metal surface when the flow rate of a process stream within a flow line ranges between 0-50 m/sec. Preferably, the aminoalkyl imidazolines of this invention mainly suppresses an anodic reaction of the metal corrosive process, and maintain adhesion to said metal surface when the flow rate of a process stream within a flow line ranges between 10-30 m/sec.

As used herein the term “alkenyl” is a monovalent group derived from a straight or branched chain hydrocarbon containing one or more carbon-carbon double bonds. Illustrative alkenyl groups include, but are not limited to, groups such as ethenyl, propenyl, butenyl, and 1-methyl-2-buten-1-yl.

As used herein the term “alkoxy” is an alkyl-O-group where alkyl is defined herein. Illustrative alkoxy groups include, but are not limited to, groups such as methoxy, ethoxy, propoxy, butoxy, octyloxy, dodecyloxy and octadecyloxy. Related to alkoxy groups are “aryloxy” groups, which have an aryl group singular bonded to oxygen such as the phenoxy group (C₆H₅O—).

As used herein the term “alkyl” is a monovalent group derived from a straight or branched chain saturated hydrocarbon by the removal of a single hydrogen atom. Illustrative alkyl groups include, but are not limited to, groups such as ethyl, n- and iso-propyl, n-, sec-, iso- and tert-butyl, lauryl, octyl, dodecyl, and octadecyl.

As used herein the term “alkylaryl” an alkyl-arylene-group where alkyl and arylene are defined herein. Illustrative alkylaryl groups include, but are not limited to, groups such as tolyl, ethylphenyl, propylphenyl, 4-(octyloxy)benzonitrile, 4-(dodecyloxy)benzonitrile, and 4-(octadecyloxy)benzonitrile.

As used herein the term “alkylene” is a divalent group derived from a straight or branched chain saturated hydrocarbon by the removal of two hydrogen atoms. Illustrative alkylene groups include, but are not limited to, groups such as methylene, ethylene, propylene, and isobutylene.

As used herein the term “amino” is a group of formula Y¹Y²N— and quaternary salts thereof where Y¹ and Y² are independently hydrogen, alkyl, aryl, heterocycyl or arylalkyl as defined herein. Y¹ and Y², together with the N atom to which they are attached may also form a heterocyclyl group. Illustrative amino groups include, but are not limited to, groups such as amino (—NH₂), methylamino, ethylamino, iso-propylamino, tert-butylamino, dimethylamino, diethylamino, methylethylamino, and piperidino.

As used herein the term “aminoalkyl” is an amino-alkylene-group wherein amino and alkylene are defined herein. Illustrative aminoalkyl groups include, but are not limited to, groups such as 3-dimethylaminopropyl, and dimethylaminoethyl.

As used herein the term “aminoaryl” is an amino-arylene-group where amino and arylene are defined herein.

As used herein the term “aryl” means substituted and un-substituted aromatic carbocyclic radicals and substituted and un-substituted aromatic heterocyclic radicals having 5 to 10 ring atoms. Illustrative aryl groups include, but are not limited to groups such as phenyl, and naphthyl.

The aryl may optionally be substituted with one or more groups selected from, but not limited to, groups such as hydroxyl, halogen, C₁-C₁₈ alkyl, C₁-C₃₀ thiol alkyl and C₁-C₃₀ alkoxy; wherein said alkyl and thiol alkyl is preferably selected from the group consisting of a C₅-C₂₀ alkyl; most preferably from the group consisting of a C₈-C₁₈ alkyl.

As used herein the term “arylalkyl” is an aryl-alkylene-group wherein aryl and alkylene are defined herein. Representative arylalkyl include, but are not limited to, benzyl, phenylethyl, phenylpropyl, and 1-naphthylmethyl.

As used herein, the term “arylene” is a substituent of an organic compound that is derived from an aromatic hydrocarbon (arene) that has had a hydrogen atom removed from a ring carbon atom. Representative arylene include, but are not limited to, phenylene.

As used herein, the term “heterocyclyl” means an aromatic or non-aromatic monocyclic or multicyclic ring system of about 3 to about 10 ring atoms, preferably about 5 to about 10 ring atoms, in which one or more of the atoms in the ring system is/are element(s) other than carbon, for example nitrogen, oxygen or sulfur. Preferred ring sizes of rings of the ring system include about 5 to about 6 ring atoms. The heterocyclyl is optionally substituted by one or more hydroxy, alkoxy, amino or thiol groups. Representative heterocyclyl rings include, but are not limited to, piperidyl, pyrrolidinyl, piperazinyl, and morpholinyl.

“Preventing” includes preventing, inhibiting, mitigating and reducing.

Imidazolines comprise a class of nitrogen-containing heterocycles formally derived from imidazoles by the addition of hydrogen (H₂) across one of two double bonds. The 2-imidazoline (dihydroimidazole) of the disclosure contains an imine center, and is one of three isomers with the formula C₃H₆N₂.

The 2-imidazoline compound as disclosed herein is substituted at the 5-N position and the 1-C position of the 2-imidazoline ring with the following chemical groups, respectively:

-   -   a. A nitrogen containing functional group selected from the         group comprising: an amine, defined as a functional group that         contains a basic nitrogen atom with a lone pair of electrons; a         diamine, comprising a type of polyamine with two amino groups;         or a polyamine, comprising two or more primary amino groups.         Herein, the nitrogen containing functional group is defined as:

wherein m is an integer of 1 to 10 and R is a C₁-C₆ alkylene;

-   -   b. A phenyl ether (phenyl-O—R′₅) or phenyl thiol ether         (phenyl-S—R′₅)

-   -    wherein said phenyl ether comprises a phenyl group         p-substituted with orientation to said 2-imidazoline group with         an O—R′₅ group; wherein is selected from the group comprising a         C₁-C₃₀ alkyl group; more preferably a C₅-C₂₀ alkyl group, more         preferably a C₁₀-C₁₅ alkyl group, more preferably a C₁₂-C₁₆         alkyl group, most preferably a C₈-C₁₈ alkyl group, so as to         provide a p-alkoxy phenyl pendant, or:         -   wherein said phenyl thiol ether comprises a phenyl group             p-substituted with orientation to said 2-imidazoline group             with an S—R′₅ group; wherein R′₅ is selected from the group             comprising a C₁-C₃₀ alkyl group; more preferably a C₅-C₂₀             alkyl group, most preferably a C₈-C₁₈ alkyl group so as to             provide a p-thiol alkyl phenyl pendant.

As previously defined herein, the structure of the aminoalkyl imidazolines of this disclosure comprise a:

2-imidazoline substituted with:

-   -   an amine, diamine, polyamine, or repeating units thereof, at the         5-N position of the imidazoline ring; and     -   a p-alkoxy phenyl, or     -   a p-thiol alkyl phenyl pendant.

The preferred structure of the compound as disclosed herein comprises:

-   -   2-imidazoline substituted with:     -   ethanamine or N¹-(2-aminoethyl)-N²ethylethane-1,2-diamine at the         5-N position of the imidazoline ring,

and a phenyl ether or a phenyl thiol ether group at the 1-C position of the 2-imidazoline ring;

-   -   wherein said phenyl ether is para-bonded to an alkyl group         selected from the group consisting of a C₈, C₁₂ or C₁₈ alkyl so         as to form a p-octyloxy-, p-dodecyloxy, or p-octadecyloxy-phenyl         pendant, or     -   wherein said phenyl thiol ether is para-bonded to an alkyl group         selected from the group consisting of a C₈, C₁₂ or C₁₈ alkyl so         as to form a p-octyl(phenyl)sulfane, p-dodecyl(phenyl)sulfane,         or p-octadecyl(phenyl)sulfane pendant.

It is also within the scope of the disclosure to provide further substitutions onto the imidazoline, phenyl and/or phenoxy ring(s) so as to provide a structure comprising the formula:

wherein m is an integer of 1 to 10; R is a C₁-C₆ alkylene; preferably a branched or linear ethylene —CH₂CH₂—, propylene —CH₂CH₂CH₂—, butylene —CH₂CH₂CH₂CH₂—, or pentylene —CH₂CH₂CH₂CH₂CH₂— group,

X is a heteroatom independently selected from the group consisting of oxygen and sulfur;

R′₁ thru R′₅ are each independently selected from the group consisting of hydrogen, C₁-C₃₀ alkyl, alkenyl, aryl, alkylaryl, arylalkyl, aminoalkyl, and aminoaryl, preferably R′₁-R′₄ are hydrogen atoms and R′₅ is a C₆-C₈ alkyl group, more preferably a C₁₀-C₃₀ alkyl group, more preferably a C₁₂-C₁₈ alkyl group, most preferably a C₁₄-C₁₆ alkyl group;

R₂ and R₃ are each independently selected from the group consisting of hydrogen, hydroxyl, halogen, C₁-C₃₀ alkyl, alkenyl, aryl, alkylaryl, arylalkyl, aminoalkyl, aminoaryl, (CH₂)₂COOH, CH₂CH(CH₃)COOH and imidazoline, preferably R₂ and R₃ are hydrogen atoms.

Specific compounds encompassed by the general formula include:

1-(2-aminoethyl)-2-(4-octyloxyphenyl)-2-imidazoline, 1-(2-aminoethyl)-2-(4-odecyloxyphenyl)-2-imidazoline, 1-(2-aminoethyl)-2-(4-octadecyloxyphenyl)-2-imidazoline, 1-[2-{2-(2-aminoethylamino)ethylamino}ethyl]-2-(4-octyloxyphenyl)-2-imidazoline, 1-[2-{2-(2-aminoethylamino)ethylamino}ethyl]-2-(4-dodecyloxyphenyl)-2-imidazoline, and 1-[2-{2-(2-aminoethylamino)ethylamino}ethyl]-2-(4-octadecyloxyphenyl)-2-imidazoline.

The compounds of the present invention may include stereoisomers such as optical isomers, diastereoisomers and geometrical isomers, or tautomers depending upon the mode of substituents. Thus, the compounds of the present disclosure include all of the stereoisomers, tautomers, and a mixture thereof.

Also, polymorphs, hydrates, and solvates of the compounds of the present disclosure are included within the scope of the disclosure.

The synthesis process used to prepare the aminoalkyl imidazolines of this disclosure initially involve the preparation of alkyloxybenzoic acids having a formula of R—O—R′CO₂H wherein R is C₂-C₃₀ alkyl or alkenyl, and R′ is an optionally substituted aryl group. The R hydrophobe is selected from the group comprising a C₁-C₃₀ alkyl; preferably a C₅-C₂₀ alkyl, most preferably a C₈-C₁₈ alkyl. The alkyloxybenzoic acids are further reacted to obtain an alkoxybenzamide, which is subsequently reacted to obtain an alkoxybenzonitrile. The use of the alkoxybenzonitrile as a starting material for the synthesis of a series of aminoalkyl imidazolines is described herein. Furthermore, the corrosion inhibition properties of said compounds are also presented herein.

The syntheses of the class of imidazolines from p-alkoxybenzonitrile and oligoamines H₂N(CH₂CH₂NH)_(n)—H (n=2 and 4) are outlined in Scheme 2, wherein R is selected from the group consisting of C₈H₁₇, C₁₂H₂₅, and C₁₈H₃₇. Starting nitriles, 4-(octyloxy)benzonitrile (a), 4-(dodecyloxy)benzonitrile (b), and 4-(octadecyloxy)benzonitrile (c) are shown below.

Polyalkylene polyamines used to prepare the aminoalkyl imidazolines of this disclosure have the formula

where R is C₁-C₆ alkylene and m is an of 1 to 10. “Polyethylene polyamine” means a polyalkylene polyamine where R is —CH₂CH₂—. Representative polyalkylene polyamines include diethylene triamine (DETA), triethylene tetramine, tripropylene tetramine, tetraethylene pentamine (TEPA), and pentaethylene hexamine.

Herein an aminoalkyl imidazoline is prepared by reacting an alkoxybenzonitrile with diethylene triamine (DETA) in an exact 1:2.5 mmolar ratio to yield an 1-(2-aminoethyl)-2-(4-octyloxyphenyl)-2-imidazoline (VIIIa), an 1-(2-aminoethyl)-2-(4-dodecyloxyphenyl)-2-imidazoline (VIIIb), or an 1-(2-aminoethyl)-2-(4-octadecyloxyphenyl)-2-imidazoline (VIIIc).

Further herein, an aminoalkyl imidazoline is prepared by reacting an alkoxybenzonitrile with tetraethylene pentamine (TEPA) in an exact 1:2.5 mmolar ratio to yield an 1-[2-{2-(2-aminoethylamino)ethylamino}ethyl]-2-(4-octyloxyphenyl)-2-imidazoline (IXa), 1-[2-{2-(2aminoethylamino) ethylamino}ethyl]-2-(4-dodecyloxyphenyl)-2-imidazoline (IXb), or an 1-[2-{2-(2-aminoethylamino) ethylamino}ethyl]-2-(4-octadecyloxyphenyl)-2-imidazoline (IXc).

An electron-rich p-alkoxyphenyl substituent at the carbon atom of the N═C—N group augments the electron-donor capacity of the N═C—N group; as such, the effect of increasing electron density of the ring-nitrogens on their inhibition efficacies was examined. The alkoxy groups of C₈, C₁₂ and C₁₈ alkyl chairs were chosen to demonstrate the importance of hydrophobe chain length on the inhibition of CO₂ corrosion. The N-pendent groups of CH₂CH₂NH₂ and (CH₂CH₂NH)₂CH₂CH₂NH₂, allow comparison of these chains and their role in the suppression of the corrosion of mild steel in CO₂/0.5 M NaCl solutions. The corrosion inhibition studies of this disclosure utilized potentiodynamic polarizations, gravimetric weight loss and X-ray photoelectron spectroscopy (XPS) to assist in clarifying the inhibition mechanism.

One common structural component in the imidazolines of this disclosure is the placement of an aromatic ring in conjunction with the N═C—N group. This allows the shifting of the charge density from the electron-rich benzene ring to the imidazolines as shown using structure VIII (Scheme 2). This stabilizing electron movement results in the two rings becoming coplanar. As a result, the electron-rich N═C—N groups, along with the aromatic π-clouds, are thought to undergo strong adsorption by the formation of coordinate-type bonds with the empty d-orbitals of Fe on the anodic sites of the metal surface. The highly surface-active imidazolines VIII and IX disclosed herein demonstrated superior corrosion inhibition in a CO₂-saturated 0.5 M NaCl, as illustrated in the following tables.

TABLE 1 Results of Tafel plots of a mild steel sample in various solutions containing inhibitors VIIIa-VIIIc in 0.5M NaCl saturated with CO₂ at 40° C. Tafel plots E_(corr) β_(a) Temp Conc. vs. SCE (mV/ β_(C) i_(corr) η Sample ° C. (ppm) (mV) dec) (mV/dec) (μA/cm²) (%)^(a) Blank^(b) 40 0 −700 41.2 −258 103.6 — VIIIa 40 1 −694 75.2 −141 49.9 51.8 5 −683 40.0 −166 38.5 62.8 10 −677 44.3 −172 30.9 70.1 20 −671 63.9 −181 24.6 76.2 50 −667 45.6 −139 17.3 83.3 100 −665 36.4 −123 8.32 92.0 VIIIb 40 1 −691 25.0 −113 51.1 50.7 5 −674 30.9 −128 36.9 64.4 10 −664 23.1 −120 26.9 74.0 20 −655 28.9 −136 19.7 80.9 50 −646 25.4 −115 9.68 90.6 100 −619 33.1 −127 7.55 92.7 VIIIc 30 0 −692 46.2 −137 93.4 — 1 −686 26.1 −119 43.1 53.8 2 −677 33.2 −148 39.1 58.1 3 −663 28.8 −142 36.0 61.4 5 −656 25.7 −156 26.7 71.4 10 −651 41.3 −149 21.6 76.8 20 −630 30.8 −126 8.9 90.4 40 1 −683 25.5 −114 43.1 58.4 5 −672 34.3 −117 28.3 72.7 10 −659 47.1 −187 20.8 79.9 20 −651 51.4 −157 8.69 91.6 50 −636 39.2 −148 4.81 95.4 100 −620 43.8 −167 1.97 98.1 50 0 −743 39.2 −157 124.1 — 1 −728 47.1 −128 65.2 47.5 2 −716 38.5 −146 61.1 50.7 3 −700 24.8 −162 56.7 54.2 5 −689 32.3 −125 39.2 68.3 10 −681 29.4 −149 31.6 74.5 20 −663 37.7 −153 16.3 86.8 ^(a)Inhibition Efficiency, IE (i.e., η) = surface coverage θ. ^(b)The blank was a 0.5M NaCl solution saturated with CO₂. ^(c)Inhibitor sample was dissolve in 0.5 cm³ 2-propanol, and added with 249.5 cm³ blank solution.

TABLE 2 Results of Tafel plots of a mild steel sample in various solutions containing inhibitors IXa-IXc in 0.5M NaCl saturated with CO₂ at 40° C. Tafel plots E_(corr) β_(a) Temp Conc. vs. SCE (mV/ β_(C) i_(corr) η Sample ° C. (ppm) (mV) dec) (mV/dec) (μA/cm²) (%)^(a) Blank^(b) 40 0 −700 41.2 −258 103.6 — IXa 40 1 −671 61.1 −249 49.2 52.5 5 −660 32.4 −146 41.2 60.3 10 −648 57.5 −228 29.1 71.9 20 −645 35.8 −183 22.5 78.2 50 −641 69.2 −124 19.6 81.1 100 −637 66.7 −238 9.2 91.1 IXb 40 1 −662 38.1 −204 47.2 54.4 5 −643 47.2 −260 32.7 68.4 10 −633 35.2 −168 26.4 74.5 20 −625 56.2 −154 19.5 81.2 50 −609 45.9 −197 14.1 86.5 100 −605 41.8 −191 6.35 93.8 IXc 30 0 −692 46.2 −137 93.4 — 1 −683 29.8 −125 42.8 54.1 2 −674 42.7 −156 35.2 62.4 3 −659 38.5 −129 28.7 69.3 5 −654 42.1 −148 20.0 78.5 10 −633 33.0 −134 14.2 84.8 20 −615 36.5 −149 4.13 95.6 40 1 −668 54.5 −235 45.3 56.3 5 −657 73.1 −194 26.1 74.8 10 −645 87.2 −293 20.8 79.9 20 −619 34.6 −148 6.91 93.3 50 −598 37.6 −176 2.82 97.2 100 −590 40.6 −212 1.97 98.1 50 0 −743 39.2 −157 124.1 — 1 −711 52.1 −153 62.6 49.5 2 −694 39.4 −139 57.8 53.4 3 −671 42.6 −116 44.9 63.8 5 −660 29.3 −152 36.2 70.8 10 −638 38.0 −134 28.6 76.9 20 −626 31.9 −148 11.4 90.7 ^(a)Inhibition Efficiency, IE (i.e., η) = surface coverage θ. ^(b)The blank was a 0.5M NaCl solution saturated with CO₂. ^(c)Inhibitor sample was dissolve in 0.5 cm³ 2-propanol, and added with 249.5 cm³ blank solution.

The LPR study revealed θ% values of 73.6, 76.9, and 88.9 at a concentration of 20 ppm of the DETA-derived imidazolines VIIIa, VIIIb, and VIIIc respectively (Table 3).

TABLE 3 Results of LPR method in 0.5M NaCl saturated with CO₂ at 40° C. Polarization resistance Temp Concentration R′_(p) Sample ° C. (ppm by weight) (Ω cm²) θ^(a) θ (%) Blank^(b) 40 0 89.7 — — VIIIa 40 1 218 0.589 58.9 5 247 0.637 63.7 10 276 0.675 67.5 20 340 0.736 73.6 50 568 0.842 84.2 100 973 0.908 90.8 VIIIb 40 1 194 0.538 53.8 5 290 0.691 69.1 10 315 0.715 71.5 20 388 0.769 76.9 50 653 0.863 86.3 100 1059 0.915 91.5 VIIIc 30 0 82.3 — — 1 165 0.502 50.2 2 192 0.572 57.2 3 226 0.635 63.5 5 301 0.726 72.6 10 471 0.825 82.5 20 1107 0.925 92.5 40 1 210 0.573 57.3 5 305 0.706 70.6 10 477 0.812 81.2 20 809 0.889 88.9 50 1317 0.932 93.2 100 1800 0.950 95.0 50 0 97.8 — — 1 172 0.431 43.1 2 196 0.500 50.0 3 218 0.552 55.2 5 297 0.671 67.1 10 451 0.783 78.3 20 689 0.858 85.8 ^(a)Surface coverage, θ = Inhibition Efficiency, IE (i.e., η). ^(b)0.5M NaCl solution saturated with CO₂.

For the corresponding TEPA-derived imidazolines IXa, IXb and IXc, the respective θ% at 20 ppm were found to be 74.7, 82.4, and 91.2 (Table 4).

TABLE 4 Results of LPR method in 0.5M NaCl saturated with CO₂ at 40° C. Polarization resistance Temp Concentration R′_(p) Sample ° C. (ppm by weight) (Ω cm²) θ^(a) θ (%) Blank^(b) 40 0 89.7 — — IXa 40 1 162 0.446 44.6 5 214 0.581 58.1 10 281 0.681 68.1 20 355 0.747 74.7 50 515 0.826 82.6 100 918 0.902 90.2 IXb 40 1 212 0.577 57.7 5 260 0.655 65.5 10 332 0.730 73.0 20 509 0.824 82.4 50 540 0.834 83.4 100 1181 0.924 92.4 IXc 30 0 82.3 — — 1 169 0.514 51.4 2 213 0.613 61.3 3 256 0.678 67.8 5 336 0.755 75.5 10 592 0.861 86.1 20 2562 0.968 96.8 40 1 176 0.493 49.3 5 386 0.768 76.8 10 616 0.854 85.4 20 1019 0.912 91.2 50 1695 0.947 94.7 100 2045 0.956 95.6 50 0 97.8 — — 1 197 0.504 50.4 2 225 0.565 56.5 3 274 0.643 64.3 5 313 0.687 68.7 10 546 0.821 82.1 20 902 0.892 89.2 ^(a)Surface coverage, θ = Inhibition Efficiency, IE (i.e., η). ^(b)0.5M NaCl solution saturated with CO₂.

At various concentrations of the inhibitors, the pentamine derivatives IX imparted slightly better inhibition efficiencies than their triamine counterparts VIII. Note that a concentration of 20 ppm of VIIIa, VIIIb, VIIIc and IXa, IXb, IXc translates into their respective concentrations of 63.0, 53.5, 43.7, 49.6, 43.5, and 36.8 μM respectively.

A higher polyamine chain length seems to augment the corrosion inhibition to a limited extent. Both VIIIc and IXc having a hydrophobic alkyl chain of C₁₈ show better inhibition efficacies than their respective C₈ or C₁₂ counterparts VIIIa, IXa, and VIIIb, IXb. An increase in the θ% values with an increasing alkyl chain length may be attributed to the extra coverage of the metal surface made possible by the longer hydrophobic tails. The results of the Tafel extrapolations (Tables 1 and 2) corroborated the findings of the LPR method (Tables 3 and 4). As evident from Table 5, at a concentration of 100 ppm, all the imidazolines imparte very good IEs, especially VIIIc and IXc, where both have a η% of over 98.

TABLE 5 Corrosion inhibition efficiency, η (%) using polarization resistance and Tafel plots of mild steel samples in various solutions containing 50 and 100 ppm by weight of the inhibitors in 0.5M NaCl solution saturated with CO₂ (1 atm) at 40° C. η (%) Polarization method Tafel method Compound 20^(a) 50^(a) 100^(a) 20^(a) 50^(a) 100^(a) VIIIa 73.6 84.2 90.8 76.2 83.3 92.0 VIIIb 76.9 86.3 91.5 80.9 90.6 92.7 VIIIc 88.9 93.2 95.0 91.6 95.4 98.1 IXa 74.7 82.6 90.2 78.2 81.1 91.1 IXb 82.4 83.4 92.4 81.2 86.5 93.8 IXc 91.2 94.7 95.6 93.3 97.2 98.1 ^(a)inhibitor concentration in ppm by weight

Referring now to FIGS. 5A, 5B, 5C, and 5D which shows the Tafel plots for the imidazolines and their Tafel constants, while corrosion potentials and IEs are included in Tables 1 and 2. The E_(corr) values in all the cases progressively shifted to less negative values (i.e. noble direction) with the increase in the inhibitor concentrations, thereby indicating that the imidazolines are suppressing mainly the anodic reactions as illustrated in FIGS. 5A, 5B, 5C, and 5D. A difference of E_(corr) values between the blank and inhibited solution (100 ppm) in the ranges 35-72 mV (Table 1) and 57-78 mV (Table 2) for (VIIIa, VIIIb, VIIIc) and (IXa, IXb, IXc), respectively, does not qualify these inhibitors to be classified under anodic type inhibitors. Classification of a compound as a cathodic- or anodic-type inhibitor is feasible when the E_(corr) is shifted by at least 85 mV [S. Z. Dunn, Y. L. Tao, Interface Chemistry. Higher Education Press, Beijing, 1990, pp. 124-126. Incorporated herein by reference in its entirety]. Inhibitor action is more pronounced in the anodic Tafel lines as the difference between the anodic current densities in the absence and presence of inhibitor are much greater than the corresponding differences in the cathodic branches as shown in FIGS. 5A, 5B, 5C, and 5D. The inhibitors thus retard the anodic dissolution of iron more than the cathodic hydrogen evolution reaction. As evident from Tables 1 and 2, the cathodic (β_(c)) and anodic (β_(a)) slopes in most instances are not greatly affected, thereby implying that the mechanism of the reactions occuring at the electrodes are not altered in the presence of the inhibitors. The inhibitors simply block the anodic and cathodic reaction sites. The E_(corr) shifts suggest that the studied compounds in CO₂ saturated 0.5 M solution act as mixed-type inhibitors under the predominance of anodic control. FIGS. 5A, 5B, 5C, and 5D shows that the shift in the anodic direction increases in the order: VIIIa<VIIIb<VIIIc and IXa<IXb<IXc, and the shift in the presence of a pentaamine-derived inhibitor (IX) were found to be slightly higher than those of a triamine-derived imidazolines (VIII). The negative values of ΔH°_(ads) suggest an exothermic physisorption of the inhibitors on the metal surafce, while negative ΔG°_(ads) certify their favorabilty as illustrated in Table 6. [S. Nesic, G. T. Solvi, J. Enerhaug, Comparison of the rotating cylinder and pipe flow tests for flow-sensitive carbon dioxide corrosion, Corrosion 10 (1995) 51773-787. Incorporated herein in its entirety.] The relatively smaller values of −ΔG°_(ads) values in the range 37-43 kJ/mol, which are greater than 20 kJ/mol, indicate the electrostatic (i.e. physisorption) and chemisorption adsorption mechanism of the imidazolines on mild steel [W. Durnie, R. De Marco, A. Jefferson, B. Kinsella, Development of a structure-activity relationship for oil field corrosion inhibitors, J. Electrochem. Soc. 146 (1999) 1751-1756. S. Z. Duan, Y. L. Tao, Interface Chemistry. Higher Education Press, Beijing, 1990, pp. 124-126. Incorporated herein by reference in its entirety].

A protective film can be constructed by the formation of at least one ‘coordinate type’ chemical bond between d-orbitals of iron and the non-bonding, as well as the π-electrons, in the electron-rich imidazoline group and the aromatic ring. [F. Bentiss, M. Triasnel, M. Lagrenee, The substituted 1,3,4-oxadiazoles: a new class of corrosion inhibitors of mild steel in acidic media. Corros. Sci., 42 (2000) 127-146 S. Kertit, B. Hammouti, Corrosion inhibition of iron in 1 M HCl by 1-phenyl-5-mercapto-1,2,3,4-tetrazole. Appl. Surf. Sci., 93 (1996) 59-66. Incorporated herein by reference in their entirety].

Moderately positive values for the entropy change, ΔS°_(ads), ascertain the favorable increase in randomness as a result of the displacement of water molecules from the metal surface as shown in Table 6. As the temperature increases, the E_(corr) becomes more negative (less noble), which makes the metal surface more susceptible to media attack.

TABLE 6 The values of the adsorption equilibrium constant from Langmuir adsorption isotherms and free energy, enthalpy, entropy changes of the mild steel dissolution in the presence of inhibitors VIII and IX in CO₂ saturated 0.5M NaCl at various temperatures. Temp K_(ads) × 10⁻⁵ ΔG°_(ads) ΔH°_(ads) ΔS°_(ads) Compound (° C.) (L mol⁻¹)^(a) (kJ mol⁻¹) (kJ mol⁻¹) (J mol⁻¹ K⁻¹) VIIIa 40 27083 −37.0 — — VIIIb 40 34995 −37.7 — — VIIIc 30 191106 −40.8 −15.8 +82.5 40 163330 −41.7 50 129573 −42.4 IXa 40 32676 −37.5 — — IXb 40 81241 −39.9 — — IXc 30 310441 −42.0 40 266094 −43.0 −16.3 +85.0 50 210417 −43.7 ^(a)K_(ads) obtained in L/mg was converted to L/mol

Some of the anodic polarization curves in the current-vs-potential plots, especially in the higher concentration range of the inhibitors, have a current-increasing plateau which is called the desorption potentials. [F. Bentiss, M. Triasnel, M. Lagrenee, The substituted 1,3,4-oxadiazoles: a new class of corrosion inhibitors of mild steel in acidic media. Corros. Sci., 42 (2000) 127-146 W. Jia, A study on the impedance responses of inhibitor desorption, Chin. J. Oceanol. Limnol. 16 (1998) 54-59. Incorporated herein by reference in their entirety.] This is displayed in FIGS. 5A, 5B, 5C, and 5D. Significant steel dissolution occurs at potentials higher than the respective desorption potential, thereby suggesting a mechanism by which the inhibitors block the anodic sites on the metal surface. The surface coverage data (θ) indicate that the adsorption of the imidazolines are fitted best by the Langmuir adsorption isotherm; while some of them followed Temkin as well as Freundlich adsorption isotherms (Table 7).

TABLE 7 Square of coefficient of correlation (R²) and values of the constants in the adsorption isotherms of Temkin, Frumkin, Langmuir and Freundlich in the presence of inhibitors VIII and IX in CO₂ Saturated 0.5M NaCl solution (LPR data used for the isotherm). Com- Temp Temkin Langmuir Frumkin Freundlich pound (° C.) (R², f) (R²) (R², a) (R²) VIIIa 40 0.9260, 14 0.9984 0.7313, −3.5 0.9503 VIIIb 40 0.9912, 12 0.9956 0.9387, −3.2 0.9843 VIIIc 30 0.9901, 6.9 0.9992 0.8389, −1.1 0.9952 40 0.9831, 9.4 0.9971 0.8128, −1.9 0.9929 50 0.9848, 6.6 0.9940 0.8105, −0.85 0.9822 IXa 40 0.9954, 10 0.9919 0.9542, −2.4 0.9864 IXb 40 0.9338, 13 0.9936 0.7907, −3.4 0.9573 IXc 30 0.9997, 6.6 0.9972 0.8551, −0.78 0.9948 40 0.9808, 7.0 0.9968 0.9961, −0.73 0.9591 50 0.9874, 7.4 0.9967 0.7608, −0.99 0.9881

The relatively higher values of the energetic inhomogeneity factor f obtained from the Temkin model signifies a strong dependence of the free energy of adsorption (ΔG°_(ads)) on the surface coverage. [B. I. Podlovchenko, B. B. Damaskin, Possible demarcation of adsorption isotherms based on repulsive interaction and surface inhomogeneity, Elektrokhimiya 8 (1972) 297. A. E. Stoyanova, E. I. Sokolova, S. N. Raicheva, The inhibition of mild steel corrosion in 1 M HCl in the presence of linear and cyclic thiocarbamides—Effect of concentration and temperature of the corrosion medium on their protective action, Corros. Sci. 39 (1997) 1595-1604. Incorporated herein by reference in their entirety.]

The imidazolines performed very well at higher temperature (120° C.) and pressure 10 bar, CO₂) to arrest corrosion in 0.5M NaCl (Table 8).

TABLE 8 Corrosion rates and inhibition efficiencies of various corrosion inhibitors (200 ppm by weight) at 120° C. and 10 bar pressure of CO₂ in 0.5M NaCl solution. CR^(b) Average % Solution Coupon^(a) (mm y⁻¹) % Inhibition Inhibition Blank A 2.19 — — B 2.23 — VIIIa A 0.607 72.3 71.8 B 0.638 71.4 VIIIb A 0.195 91.1 90.8 B 0.212 90.5 VIIIc A 0.149 93.2 93.1 B 0.156 93.0 IXa A 0.569 74.0 72.5 B 0.647 71.0 IXb A 0.153 93.0 92.4 B 0.181 91.9 IXc A 0.153 93.0 93.3 B 0.143 93.6 Q I 80 A 0.429 80.4 81.0 B 0.410 81.6 ARMOHIB29 A 0.396 81.9 82.7 B 0.368 83.5 ^(a)Two mild steel coupons A and B having different carbon content and compositions ^(b)Corrosion rate

The inhibition efficacy η% of the imidazolines, as determined using two types of metal coupons A and B having different elemental compositions and carbon content, were found to increase in the following order: VIIIc>VIIIb>VIIIa> and IXc>IXb>IXa. The current imidazolines having C₁₂ (VIIIb, IXb) and C₁₈ (VIIIc, IXc) alkyl chains, outperformed the two commercial imidazolines QI80 and ARMOHIB219 (Table 8). The objective of constructing a surface tension versus inhibitor concentration profile is to find the imidazoline's CMC which can be used to compare the absorption pattern on either side of the CMC. The imidazolines, when found in an aqueous media, are classified as cationic surfactants because of the involvement of the cationic form B found in equilibrium with its neutral counterpart A (Scheme 1). [D. Bajpai, V. K. Tyagi, Fatty imidazolines: chemistry, synthesis, properties and their industrial application, J. Oleo. Sci. 55 (7) (2006) 319-329. Incorporated herein by reference in its entirety].

In terms of molar concentration, the CMC, well as surface tension of the imidazolines, are found to follow the order if: VIIIa>VIIIb>VIIIc; IXa>IXb>IXc; and VIII>IX (Table 9). In an aqueous 0.5 M NaCl solution the pentamine derivatives IX a-c, having greater hydrophilic polar heads, are expected to have greater CMC values for being more soluble in water as compared to their triamine counterparts. The increase in the hydrophobic alkyl chain length decreases the solubility of the imidazolines, and, as expected, decreases the CMC. [W. Wang, M. L. Free, D. Horsup, Prediction and measurement of corrosion inhibition of mild steel by imidazolines in brine solutions. Metall. Mater. Trans. B, 36 (2005) 335-341. Incorporated herein by reference in its entirety.] The C₁₈ alkyl tails, by virtue of having the greater hydrophobic interactions, lead to smaller CMC values for the imidazolines VIIIc and IXc. Imidazoline VIIIa CO₂-saturated 0.5 NaCl has a CMC value of 37.4 μM (≈11.9 ppm), whereas in the absence of CO₂, it becomes 30.2 μM (≈9.59 ppm). The formation of a carbamate salt of an imidazoline in a CO₂-saturated NaCl solution makes it more water-soluble, hence increases the CMC value (vide infra). A closer look at the CMC values FIGS. 8A and 8B and Table 9, and the surface coverage (θ) data FIGS. 8C and 8D, and Tables 3 and 4, reveals that imidazolines cover a majority of the surface before the concentrations reach their CMC values.

TABLE 9 Surface properties of imidazolines VIII and IX in 0.5M NaCl at 40° C. Surface tension C_(cmc) C_(cmc) ΔG°_(mic) Compound (mN m⁻¹) (μmol L⁻¹) (ppm) (kJ mol⁻¹) VIIIa 33.5 30.2 9.59 −27.1 VIIIa^(a) 35.0 37.4 11.9 −26.5 VIIIb 31.5 21.8 8.14 −27.9 VIIIc 29.3 20.0 9.15 −28.2 IXa 36.2 22.4 8.99 −27.9 IXb 34.0 18.3 8.38 −28.4 IXc 31.2 13.9 7.53 −29.1 ^(a)0.5M NaCl saturated with C0₂

An adsorption on the metal surface is favored over a micellization since the AG°_(ads) values are more negative (Table 6) when compared with the corresponding ΔG°_(mic) (Table 9). The monolayer formation at the interface between the metal and solution is complete before the CMC; after which multilayer coverage, as a result of adsorption of the micelles, may impart further protection albeit to a lesser degree. [4 K. Esumi, M. Ueno, Structure Performance Relationships in Surfactants. Marcel Dekker Press, 2001. Incorporated herein by reference in its entirety.]

The XPS survey scan composition of Fe immersed in an inhibited solution of 0.5 M NaCl-CO₂ revealed the presence of a carbonaceous film at the metal surface as indicated by its high carbon and small Fe contents (Table 10).

TABLE 10 XPS survey scan composition of Fe immersed in inhibited solution of 0.5M NaCl - CO₂ (1 atm) at 40° C. for 4 h. Approx. Composition binding energy (atom %) Peak (eV) 8a 8b 8c 9a 9b 9c C 1s 285.4 24.6 30.8 34.9 28.7 45.0 32.3 C 1s 286.4 37.8 32.7 24.8 22.8 19.1 24.3 O 1s 530.1 9.0 9.0 4.0 11.5 4.5 11.5 O 1s 531.5 26.5 14.4 1.6 5.7 O 1s 532.9 19.4 19.2 1.2 23 16.9 O1s 534.4 9.5 11.4 N 1s 400.0 4.7 5.2 5.0 N 1s 400.6 3.3 1.1 4.4 5.5 Fe 2p 706.3 0.2 0.4 Fe 2p 711.0 1.4 1.9 2.3 4.2 1.5 3.3 Fe 2p 714.3 0.78 0.4 0.6 0.8 0.5 0.5 Cl 2p 197.55 0.92 1.7 199.19

The presence of N (Nitrogen) points (FIGS. 9C, 9F, 10C) its origin to the imidazolines: the metal surface is thus covered by a film of imidazolines. The XPS spectra, for example, in the presence of inhibitors VIIIc and IXc, are shown in FIG. 9A and FIG. 9D, respectively.

The XPS deconvoluted profiles of a C 1 s spectrum for VIIIc and IXc revealed a two-peak profile (FIGS. 9B and 9E); the peak at 285.4 eV was assigned to the C—C aliphatic bonds, while the presence of C═C, C═O, and C—N bonds were reflected by the peak at 286.4 eV. The presence of O 1 s peaks at 530.1 and 531.5 eV is attributed to the O²⁻ in Fe₂O₃ and hydrous iron oxide FeOOH, respectively (FIG. 10A), [O. Olivares-Xometl, N. V. Likhanova, M. A. Dominguez-Aguilar, J. M. Hallen, L. S. Zamudio, E. Arce, Surface analysis of inhibitor films formed by imidazolines and amides on mild steel in an acidic environment, Appl. Surf. Sci. 252 (2006) 2139-2152. M. Tourabi, K. Nohair, M. Traisnel, C. Jama, F. Bentiss, Electrochemical and XPS studies of the corrosion inhibition of carbon steel in hydrochloric acid pickling solutions by 3,5-bis(2-thienylmethyl)-4-amino-1,2,4-triazole, Corros. Sci. 75 (2013) 123-133. Incorporated herein by reference in their entirety.] The other O 1 s peaks at 532.9 and 534.3 may be associated with the oxygen of adsorbed water. Small intensity peaks at 711 and 706.3 are indicative of the presence of Fe³⁺ (2 p) and Fe⁰ (2p) (FIG. 10B). The peak located around 714.3 is indicative of the presence of a small concentration of FeCl₃.

Imidazolines VIIIb and IXb, as shown in Scheme 3, both have hydrophobe lengths equivalent to 17 CC bonds. At concentrations of 1, 5 and 10 ppm, they are found to impart better corrosion protection than their corresponding imidazolines having heptadecyl (C₁₇) alkyl chains X and XI, respectively.

Results of the comparative inhibition behaviors of imidazolines having similar pendent chain length 8b versus 10 and 9b versus 11 are shown in Table 11 below.

TABLE 11 η % at concentration (ppm) of Imidazoline 1 5 10 20 50 VIIIb 53.8 69.1 71.5 76.9 86.3 X 23.1 54.0 64.7 — 84.5 IXb 57.7 65.5 73.0 82.4 83.4 XI <14.3 <49.9 65.4 87.2 90.2

The length of the benzene ring is considered an equivalent to four CC bonds and O is assumed to be an equivalent of C. Aminoalkyl imidazolines VIIIc and IXc, having hydrophobes equivalent to 23 CC bonds, achieved superior results when compared with imidazolines VIIIa,b and IXa,b of this disclosure (Tables 3-5).

A study to determine the chemical behavior of the imidazolines in aqueous CO₂ was performed. An initial ¹³C NMR spectra of VIIIa in CDCl₃ using TMS as an internal standard is shown in FIG. 11A. Subsequently, the chemical behavior of the imidazolines in aqueous CO₂ was investigated using the following procedure: CO₂ was passed through a mixture of VIIIa (65 mg) in D₂O (0.8 cm³) at 40° C. for 5 min. The ¹³C NMR spectrum revealed the presence of four signals at the chemical shifts of 161.0, 163.0, 164.4 and 167.3 ppm, assigned to the carbons marked as HCO₃ ⁻, i, k, and e, respectively in FIG. 11B. The assignment of HCO₃ ⁻ was based on literature [D. J. Heldebrant, P. G. Jessop, C. A. Thomas, C. A. Eckert, C. L. Liotta, The Reaction of 1,8-Diazabicyclo[5.4.0]undec-7-ene (DBU) with carbon dioxide, J. Org. Chem. 70 (2005), 5335-5338. Incorporated herein by reference in its entirety]. The presence of carbon marked ‘k’ signal at 164.4 ppm was assigned to the carbamate group [NHC(═O)O⁻]; the absence of any signal at ≈174 ppm precluded the presence of amide group [NHC(═O)C—] which would have been generated by hydrolysis of the imidazoline groups. [Y. Duda, R. G. Rueda, M. Galicia, H. I. Beltran, L. S. Z. Rivera, Corrosion inhibitors: Design, performance, and computer simulations. J. Phys. Chem. B, 109 (2005) 22674-22684. Incorporated herein by reference in its entirety.] The reaction in the presence of CO₂ is presented in Scheme 4.

Imidazoline VIIIa is expected to give rise to the bicarbonate salt VIIIa-H⁺ HCO₃ ⁻ as a result of protonation of the amidine motif; the reaction of the primary amine group (NH₂) would furthermore lead to the formation of carbamic acid. [P. N. Sutar, A. Jha, P. D. Vaidya, E. Y. Kenig, Secondary amines for CO₂ capture: A kinetic investigation using N-ethylmonoethanolamine, Chem. Eng. J. 207-208 (2012) 718-724. Incorporated herein by reference in its entirety.] In a similar experiment carried out in H₂O, the residue was subsequently vacuum dried after being treated with flowing CO₂, followed by removal of the solvent, at room temperature. The IR spectrum of the residue revealed the absence of any peak around 1640 cm⁻¹ thereby asserting that the hydrolysis of the amidine group to an amide group did not occur; the presence of a peak at 1610 cm⁻¹ indicated the presence of a protonated amidine [C═N—H⁺] W. Qiao, Z. Zheng, Q. Shi, Synthesis and properties of a series of CO2 switchable surfactants with imidazoline group, J. Surfact. Deterg. 15 (2012) 533-539. Incorporated herein by reference in its entirety.] The ¹³C NMR spectrum of the residue revealed the absence of a HCO₃ ⁻ carbon signal; however, it indicated the presence of three carbon signals at 162.5, 164.3 and 167.2 ppm which are attributed to the carbons marked i, k and e, respectively, of VIIIa-CO₂ as shown in FIG. 11B. The spectral analyses thus confirmed the formation of bicarbonate salt VIIIa, followed by bicarbonate/carbamic acid VIIIa-H⁺(HCO₃ ⁻)CO₂, (shown in FIG. 11C) in aqueous solution. However, in the absence of water, carbonic acid was lost in the form of CO₂/H₂O to give the zwitterionic carbamate VIIIa-CO₂, as indicated in FIG. 11B.

The study details the chemical reactions of imidazoline in aqueous CO₂, and confirms the effectiveness of corrosion inhibitors bearing electron-rich amidine groups.

The compounds acted mainly as anodic inhibitors, with ΔG°_(ads) values indicative of chemisorption and XPS results ascertained the formation of an adsorbed protective film in CO₂-saturated 0.5 M NaCl. The adsorption process of the imidazolines was found to obey the Langmuir adsorption isotherm. The surface coverage data and CMC values demonstrated that the inhibitor molecules have a greater tendency to undergo adsorption on to the metal surface than to form micelles. In autoclave tests under high CO₂ pressure (10 bar) and a temperature of 120° C. the imidazolines VIII b, c and IX b, c all performed superior in corrosion inhibition as compared to Q180-E and ARMOHIB 219, two commercial inhibitors tested for this purpose. These findings, as disclosed herein, confirm the function of said imidazolines incorporating electron-rich aromatic group in conjugation to the N═C—N groups.

The present disclosure relates to imidazoline compounds, a method of forming said compounds, and their use in preventing, inhibiting, corrosion.

The examples below are intended to further illustrate protocols for preparing and characterizing the various embodiments of imidazoline compounds described herein, and are not intended to limit the scope of the claims

EXAMPLE 1 Materials

Diethylenetetramine (DETA) (99.5%) and tetraethylenepentamine (TEPA) (˜60% purity) were obtained from Aldrich Chemicals. TEPA was purified as described before [M. W. S. Jawich, G. A. Oweimreen, S. A. Ali, Heptadecyl-tailed mono- and bis-imidazolines: A study of the newly synthesized compounds on the inhibition of mild steel corrosion in a carbon dioxide-saturated saline medium, Corros. Sci. 65 (2012) 104-112. Incorporated herein by reference in its entirety.] p-Hydroxybenzoic acid (I), cysteine hydrochloride, bromoalkane [R—Br (II)] and SOCl₂from Fluka Ag (Buchs, Switzerland) were used as received. All solvents were of reagent grade.

Physical Methods

All m.p.s are uncorrected. IR spectra were recorded on a Perkin Elmer 16F PC FTIR spectrometer and 1H and ¹³C NMR spectra were measured in CDCl₃ using TMS as internal standard on a JEOL LA 500 MHz NMR spectrometer. Elemental compositions were determined with an Elemental Analyzer (Carlo-Erba: Model 1106). All the reactions were carried out under N₂.

Synthesis General Procedure for the Preparation of Alkyloxybenzoic Acids (III)

Powdered NaOH (40×2.10 mmol) followed by bromoalkane 2 (40×2.16 mmol) were added to a solution of 4-hydroxybenzoic acid (40 mmol) in DMSO (100 cm³) under N₂. The reaction mixture in the closed flask was stirred using magnetic stir bar a 75° C. for 24 h. The reaction mixture was transferred into water (500 cm³) containing 15 cm³ of concentrated HCl. Crude reaction product revealed the presence of an alkyloxybenzoic acid (III) and its alkyl ester. The organic phase (extracted in ether) was washed liberally in an excess of water. The ether layer was concentrated, and the residual reaction mixture was taken up in ethanol (95% v/v) (100 cm) and added NaOH (3.00 g, 75 mmol) and heated at 70° C. for 30 min. The mixture was treated with aqueous HCl (500 cm³, 1 M). The solid product (III) was filtered and washed with water, dried and crystallized from cold pentane.

4-Octyloxybenzoic Acid (IIIa)

Yield 75.6%. Mp 92-95° C. (Found: C 71.8; H, 8.8. C₁₅H₂₂O₃ requires C, 71.97; H, 8.86%) ν_(max.) (KBr) 3502 (br), 2926, 2853, 1680, 1604, 1427, 1305, 1253, 1166, 1062, 948, 845, and 771 cm⁻¹. δ_(H) (CDCl₃) 0.89 (3 H, t, J=7.0 Hz), 1.20-1.55 (10 H, m), 1.80 (2 H, quint, J=6.8 Hz), 4.02 (2 H, t, J=6.7 Hz), 6.94 (2H, d, J=5.2 Hz,), 8.05 (2H, d, J=5.2 Hz). δ_(C) (CDCl₃): 14.08, 22.65, 25.98, 29.08, 29.21, 29.30, 31.79, 68.28, 114.18 (2 C), 121.38, 132.33 (2C), 163.70, 172.07.

4-Dodecyloxybenzoic Acid (IIIb)

Yield: 80.2% (ether). Mp 92-94° C. (Found: C, 74.5; H, 9.9. C₁₉H₃₀O₃ requires C, 74.47; H, 9.87%); ν_(max.) (KBr) 3448 (br), 2920, 2850, 1682, 1604, 1511, 1468, 1427, 1305, 1255, 1167, 946, 845 and 771 cm⁻¹. δ_(H) (CDCl₃) 0.88 (3 H, t, J=7.0 Hz), 1.10-1.55 (18 H, m), 1.81 (2 H, quint, J=6.8 Hz), 4.02 (2 H, t, J=6.8 Hz), 6.92 (2H, d, J=8.9 Hz), 8.05 (2H, d, J=8.9 Hz). δ_(C) (CDCl₃): 14.11, 22.69, 25.96, 29.08, 29.35 (2C), 29.57 (2C), 29.64 (2C), 31.91, 68.28, 114.17 (2C), 121.38, 132.33 (2C), 163.70, 172.17.

4-Octadecyloxybenzoic Acid (IIIc)

Yield: 81.3%. Mp 102-105° C. (Found: C, 76.7; H, 10.7. C₂₅H₄₂O₃ requires C, 76.87; H, 10.84%); ν_(max.) (KBr) 3448 (br), 2919, 2850 1678, 1604, 1469, 1428, 1309, 1256, 1168, 941, 845, and 771 cm⁻¹; δ_(H) (CDCl₃) 0.88 (3 H, t, J=7.0 Hz), 1.15-1.55 (30 H, m), 1.81 (2 H, quint, J=6.8 Hz), 4.02 (2 H, t, J=6.8 Hz), 6.93 (2H, d, J=8.9 Hz,), 8.05 (2H, d, J=8.9 Hz). δ_(C) (CDCl₃): 14.11, 22.69, 25.96, 29.08, 29.36 (2C), 29.70 (10 C), 31.92, 68.29, 114.19 (2 C), 121.38, 132.33 (2 C), 164.10, 171.65.

General Procedure for the Synthesis of Alkoxybenzamides (IV)

A mixture of alkoxybenzoic acid (III) (55 mmol) in SOCl₂ (15 cm³) was heated at 80° C. for 30 min. After removal of the excess SOCl₂, the residual liquid was added drop wise to a 30% NH₃ solution (150 cm³) at 0° C. The benzamide (IV) was filtered and dried.

4-Octyloxybenzamide (IVa)

Yield: 93%. MP 152-153° C. (Found: C, 72.1; H, 9.2; N, 5.5. C₁₅H₂₃NO₂ requires C, 72.25; H, 9.30; N, 5.62%); ν_(max.) (KBr) 3397, 3172, 2922, 2851, 1650, 1610, 1572, 1515, 1468, 1421 1393, 1305, 1253, 1177, 1145, 1120, 1026, 997, 853, 800, 759, 720, 644 and 620 cm⁻¹. δ_(H) (CDCl₃, 45° C.) 0.89 (3H, t, J 7.0 Hz), 1.30 (8H, m), 1.45 (2H, m), 1.79 (2H, m), 4.00 (2H, t, J 6.7 Hz) 5.80 (2H, br), 6.91 (2H, d, J 8.9 Hz), 7.76 (2H, d, J 8.9 Hz). δ_(C) (CDCl₃, 45° C.): 13.75, 22.36, 25.75, 28.91, 28.93, 29.05, 31.53, 68.07, 114.12 (2C), 125.23, 129.00 (2C), 162.05, 168.66.

4-Dodecyloxybenzamide (IVb)

Yield: 87%. Mp 143-145° C. (Found: C, 74.5; H, 10.0; N, 4.5. C₁₉H₃₁NO₂ requires C, 74.71; H, 10.23; N, 4.59%); ν_(max.) (KBr) 3387, 3179, 2921, 2851, 1647, 1611, 1572, 1516, 1469, 1421, 1395, 1308, 1256, 1175, 1145, 1120, 1019, 844, 799, 723, and 621 cm⁻¹; δ_(H) (CDCl₃, 45° C.) 0.88 (3H, t, J 7.0 Hz), 1.30 (16H, m), 1.45 (2H, m), 1.79 (2H, m), 4.00 (2H, t, J 6.7 Hz), 5.80 (2H, br), 6.91 (2H, d, J 8.9 Hz), 7.76 (2H, d, J 8.9 Hz). δ_(C) (CDCl₃, 45° C.): 14.13, 22.69, 25.98, 29.12, 29.37 (2C), 29.56, 29.59, 29.64, 29.65, 31.92, 68.23, 114.27 (2C), 125.23, 129.25 (2C), 162.23, 168.93.

4-Octadecyloxybenzamide (IVc)

Yield: 95%. Mp 138-139° C. (Found: C, 76.8; H, 10.9; N, 3.5, C₂₅H₄₃NO₂ requires C, 77.07; H, 11.12; N, 3.59%); ν_(max.) (KBr) 3426, 3195, 2919, 2849, 1649, 1616, 1577, 1515, 1471, 1424, 1397, 1307, 1252, 1180, 1145, 1120, 1035, 845, 781, and 719 cm⁻¹; δ_(H) (CDCl₃, 45° C.) 0.88 (3H, t, J 7.0 Hz), 1.27 (28H, m), 1.45 (2H, m), 1.79 (2H, m), 4.00 (2H, t, J 6.7 Hz), 5.70 (2H, br), 6.91 (2H, d, J 8.9 Hz), 7.75 (2H, d, J 8.9 Hz). δ_(C) (CDCl₃, 45° C.); 14.04, 22.66, 26.01, 29.17, 29.35 (3C), 29.68 (9C), 31.92, 68.33, 114.39 (2C), 125.23, 129.26 (2C), 162.50, 168.79.

General Procedure for the Synthesis of Alkoxybenzonitriles (V)

A mixture of alkoxybenzamide IV (45 mmol) in SOCl₂ (70 mmol) in benzene (20 cm³) was heated at 80° C. for 1 h or until the reaction was complete as indicated by TLC experiment (silica, Et₂O/MeOH 9:1). After removal of the excess SOCl₂, the residual liquid was crystallized from pentane to give the benzonitrile (V).

4-Octyloxybenzonitrile (Va)

Yield: 86%. Mp 32-34° C. (Found: C, 77.6; H, 9.1; N, 5.9. C₁₅H₂₁NO requires C, 77.88; H, 9.15; N, 6.05%); ν_(max.) (KBr) 2927, 2857, 2224, 1605, 1573, 1508, 1468, 1391, 1301, 1259, 1171, 1114, 1020, 836, and 706 cm⁻¹; δ_(H) (CDCl₃) 0.88 (3H, t, J 7.0 Hz), 1.30 (8H, m), 1.44 (2H, m), 1.78 (2H, m), 3.99 (2H, t, J 6.7 Hz), 6.92 (2H, d, J 8.9 Hz), 7.56 (2H, d, J 8.9 Hz). δ_(C) (CDCl₃): 14.01, 25.85, 28.90, 29.11, 29.19, 31.70, 68.34, 103.53, 115.10 (2C), 119.24, 133.85 (2C), 162.39.

4-Dodecyloxybenzonitrile (Vb)

Yield: 87%. Mp 49-50° C. (Found: C, 79.1; H, 9.9; N, 4.8. C₁₉H₂₉NO requires C, 79.39; H, 10.17; N, 4.87%); ν_(max.) (KBr) 2916, 2848, 2217, 1607, 1573, 1508, 1472, 1397, 1302, 1257, 1170, 1115, 1029, 1002, 832, 813, and 716 cm⁻¹; δ_(H) (CDCl₃) 0.88 (3H, t, J 7.0 Hz), 1.31 (16H, m), 1.44 (2H, m), 1.80 (2H, m), 3.99 (2H, t, J 6.7 Hz), 6.92 (2H, d, J 8.9 Hz), 7.56 (2H, d, J 8.9 Hz). δ_(C) (CDCl₃): 14.13, 22.69, 25.93, 28.97, 29.32, 29.35, 29.54, 29.57, 29.65 (2C), 31.92, 68.42, 103.61, 115.17 (2C), 119.36, 133.95 (2C), 162.46.

4-Octadecyloxybenzonitrile (Vc)

Yield: 93%. Mp 69-70° C. (Found: C; 80.6; H, 10.9; N, 3.7. C₂₅H₄₁NO requires C, 80.80; H, 11.12; N, 3.77%); ν_(max.) (KBr) 2917, 2848, 2217, 1607, 1573, 1508, 1472, 1398, 1302, 1258, 1170, 1115, 1035, 833, 812, and 718 cm⁻¹; δ_(H) (CDCl₃), 0.88 (3H, t, J 7.0 Hz), 1.28 (28H, m), 1.44 (2H, m), 1.80 (2H, m), 3.99 (2H, t, J 6.7 Hz), 6.92 (2H, d, J 8.9 Hz), 7.56 (2H, d, J 8.9 Hz). δ_(C) (CDCl₃): 14.07, 22.64, 25.87, 28.92, 29.27, 29.32, 29.48, 29.52, 29.65 (8C), 31.87, 68.35, 103.54, 115.09 (2C), 119.25, 133.86 (2C), 162.39.

General Procedure for the Synthesis of 1-(2-aminoethyl)-2-alkoxyphenyl)-2-imidazolines (VIII)

A solution of alkoxybenzonitrile (V) (25 mmol) and diethylenetriamine (VI) (DETA) (62 mmol) containing cysteine-HCl (100 mg) was heated at 145° C. for 1 h. Thereafter, another portion of cysteine-HCl (100 mg) was added and the reaction mixture was heated at 145° C. for an additional 1 h. Evolution of NH₃ gas was observed which bubbled through the connected U-tube containing mineral oil. ¹H NMR indicated the completion of the reaction. The reaction mixture was cooled and taken up in CH₂Cl₂ (50 cm³). The unreacted DETA was removed from the organic layer by washing with water (3×300 cm³); very careful agitation was required to avoid emulsion formation. Concentration of the dried (Na₂SO₄) organic layer afforded the imidazolines (VIII) as a pinkish liquid/semisolid. The imidazolines were pure as indicated by NMR spectra and used as such for the corrosion inhibition efficiency tests. The newly synthesized imidazolines gave satisfactory elemental analyses given the fact these compounds cannot be further purified by crystallization.

1-(2-Aminoethyl)-2-(4-octyloxyphenyl)-2-imidazoline (VIIIa)

Yield: 70%. ν_(max.) (neat) 3278, 2926, 2856, 1609, 1512, 1468, 1391, 1328, 1296, 1249, 1175, 1085, 1026, 950, and 839 cm⁻¹; δ_(H) (CDCl₃): 0.88 (3H, t, J 6.7 Hz), 1.20-1.50 (12H, m), 1.77 (2H, m), 2.86 (2H, t, J 6.4 Hz), 3.12 (2H, t, J 6.4 Hz), 3.43 (2H, t, J 9.5 Hz), 3.90 (2H, t, J 9.5 Hz), 3.97 (2H, t, J 6.4 Hz), 6.90 (2H, d, J 8.9 Hz), 7.50 (2H, J 8.9 Hz). δ_(C) (CDCl₃): 13.73, 22.28, 25.65, 28.84 (2C), 28.97, 31.43, 40.68, 51.10, 52.50, 52.88, 67.69, 113.92 (2C), 123.04, 129.33, (2C), 159.96, 167.52.

1-(2-Aminoethyl)-2-(4-dodecyloxyphenyl)-2-imidazoline (VIIIb)

Yield: 83%. ν_(max.) (neat) 3248, 2922, 2852, 1646, 1612, 1513, 1467, 1418, 1392, 1329, 1297, 1249, 1174, 1085, 1051, 1012, 950, 839, and 723 cm⁻¹; δ_(H) (CDCl₃): 0.88 (3H, t, J 6.7 Hz), 1.20-1.50 (20 H, m), 1.77 (2H, m), 2.85 (2H, t, J 6.4 Hz), 3.11 (2H, t, J 6.4 Hz), 3.43 (2H, t, J 9.7 Hz), 3.88 (2H, t, J 9.8 Hz), 3.96 (2H, t, J 6.4 Hz), 6.88 (2H, d, J 8.7 Hz), 7.49 (2H, J 8.7 Hz); δ_(C) (CDCl₃): 13.96, 22.51, 25.85, 29.00, 29.18, 29.22, 29.42, 29.46 (2C), 29.48, 31.73, 40.87, 51.28, 52.69, 53.08, 67.85, 114.08 (2C), 123.21, 129.41 (2C), 160.13, 167.71.

1-(2-Aminoethyl)-2-(4-octadecyloxyphenyl)-2-imidazoline (VIIIc)

Yield: 95%. ν_(max.) (KBr) 3387, 2917, 2849, 1612, 1513, 1468, 1418, 1394, 1329, 1297, 1250, 1175, 1036, 837, and 721 cm⁻¹; δ_(H) (CDCl₃): 0.88 (3H, t, J 6.7 Hz), 1.20-1.50 (32 H, m), 1.78 (2H, m), 2.85 (2H, t, J 6.1 Hz), 3.12 (2H, t, J 6.1 Hz), 3.44 (2H, t, J 9.8 Hz), 3.88 (2H, t, J 9.8 Hz), 3.96 (2H, t, J 6.4 Hz), 6.88 (2H, d, J 8.7 Hz), 7.49 (2H, J 8.7 Hz). δ_(C) (CDCl₃): 13.97, 22.53, 25.87, 29.04, 29.16, 29.21, 29.24, 29.37, 29.42, 29.45, 29.51 (2C), 29.55 (4C), 31.77, 40.86, 51.27, 52.65, 52.97, 67.88, 114.11 (2C), 123.14, 129.55 (2C), 160.19, 167.71.

General Procedure for the Synthesis of 1-[2-{2-(2-Aminoethylamino)-ethylamino}ethyl]-2-alkoxyphenyl-2-imidazolines (IX)

A solution of mono-alkoxybenzonitriles (V) (25 mmol) and tetraethylenepentamine (VII) (TEPA) (62 mmol) containing cysteine-HCl (100 mg) was heated a 145° C. for 1 h. Thereafter, another portion of cysteine-HCl (100 mg) was added and the reaction mixture was heated at 145° C. for an additional 1 h. Evolution of NH₃ gas was observed which bubbled through the connected U-tube containing mineral oil. ¹ H NMR indicated the completion of the reaction. The reaction mixture was cooled and taken up in CH₂Cl₂ (50 cm³). An equivalent workup as described under the prior general procedure for the synthesis of 1-(2-aminoethyl)-2-alkoxyphenyl)-2-imidazolines afforded the imidazolines (IX) as a pinkish liquid/semisolid. The imidazolines were pure enough as indicated by NMR spectra and used as such for the corrosion tests.

1-[2-{2-(2-Aminoethylamino)ethylamino}ethyl]-2-(4-octyloxyphenyl)-2-imidazoline (IXa)

Yield: 78%. ν_(max.) (neat) 3286, 2924, 2853, 1612, 1514, 1467, 1420, 1393, 1331, 1296, 1249, 1174, 1114, 1026, 950, 838, and 740 cm⁻¹; δ_(H) (CDCl₃): 0.89 (3H, t, J 6.7 Hz), 1.20-1.65 (14H, m), 1.77 (2H, m), 2.67 (2H, t, J 5.8 Hz), 2.73 (4H, s), 2.77 (2H, t, J 6.7 Hz), 2.80 (2H, t, J 6.0 Hz), 3.19 (2H, t, J 6.4 Hz), 3.42 (2H, t, J 9.7 Hz), 3.88 (2H, t, J 9.7 Hz), 3.96 (2H, t, J 6.4 Hz), 6.89 (2H, d, J 8.9 Hz), 7.50 (2H, J 8.9 Hz). δ_(C) (CDCl₃): 14.11, 22.64, 26.00, 29.17, 29.21, 29.33, 31.78, 41.81, 48.54, 49.25, 49.57, 49.99, 51.55, 52.51, 53.19, 68.03, 114.24 (2C), 123.37, 129.67 (2C), 160.29, 167.77.

1-[2-{2-(2-Aminoethylamino)ethylamino}ethyl]-2-(4-dodecyloxyphenyl)-2-imidazoline (IXb)

Yield: 77%. ν_(max.) (neat) 3282, 2924, 2853, 1613, 1514, 1466, 1420, 1390, 1330, 1296, 1249, 1173, 1115, 1069, 1011, 949, 838, and 735 cm⁻¹; δ_(H) (CDCl₃): 0.88 (3H, t, J 6.7 Hz), 1.20-1.70 (22H, m), 1.78 (2H, m), 2.67 (2H, t, J 5.8 Hz), 2.73 (4H, s), 2.78 (2H, t, J 6.6 Hz), 2.81 (2H, t, J 6.1 Hz), 3.19 (2H, t, J 6.4 Hz), 3.44 (2H, t, J 9.7 Hz), 3.88 (2H, t, J 9.7 Hz), 3.96 (2H, t, J 6.4 Hz), 6.89 (2H, d, J 8.9 Hz), 7.50 (2H, J 8.9 Hz). δ_(C) (CDCl₃): 14.13, 22.68, 26.02, 29.18, 29.35, 29.38, 29.60 (2C), 29.63 (2C), 31.92, 41.83, 48.56, 49.26, 49.58, 50.00, 51.57, 52.55, 53.24, 68.04, 114.25 (2C), 123.30, 129.67 (2C), 160.14, 167.78.

1-[2-{2-(2-Aminoethylamino)ethylamino}ethyl]-2-(4-octadecyloxyphenyl)-2-imidazoline (IXc)

Yield: 93%. ν_(max.) (neat) 3480, 2914, 2847, 1599, 1513, 1466, 1420, 1387, 1331, 1248, 1174, 1115, 837, and 722 cm⁻¹. δ_(H) (CDCl₃): 0.88 (3H, t, J 6.7 Hz), 1.20-1.60 (34H, m), 1.78 (2H, m), 2.68 (2H, t, J 5.5 Hz), 2.73 (4H, s), 2.78 (2H, t, J 6.5 Hz), 2.81 (2H, t, J 5.8 Hz), 3.19 (2H, t, J 6.4 Hz), 3.43 (2H, t, J 9.7 Hz), 3.88 (2H, t, J 9.7 Hz), 3.96 (2H, t, J 6.4 Hz), 6.89 (2H, d, J 8.9 Hz), 7.50 (2H, J 8.9 Hz). δ_(C) (CDCl₃): 14.14, 22.69, 26.03, 29.20, 29.37, 29.41, 29.60, 29.63, 29.70 (8C), 31.93, 41.86, 48.59, 49.29, 49.62, 50.04, 51.60, 52.58, 53.28, 68.04, 114.25 (2C), 123.42, 129.68 (2C), 160.30, 167.80.

Specimens

For the electrochemical tests, corrosion studies were carried out with mild steel coupons of the following composition: 0.089% (C), 0.037 (Cr), 0.34% (Mn), 0.022 (Ni), 0.010 (P), 0.007 (Mo), 0.005 (V), 0.005 (Cu), 99.47% (Fe). A 1 mm thick mild steel sheet was machined to a flag shape with a stem approximately 3 cm in length. Insulating the stem by araldite (affixing material) provided 2 cm² exposed area which was abraded with increasing grades of emery papers (100, 400, 600 and 1500 grit size), washed with distilled deionized water and acetone prior to drying in an oven at 110° C. The dried specimens were stored in a desiccator until being used. Immediately before use, the electrode specimens were placed in an ultrasonic bath for 5 minutes acid then washed with distilled water.

For autoclave tests, the two types of mild steel coupons A and B measuring ≈2.5×2.0×0.1 cm³ have the following composition:

Coupon A: 0.082% (C), 0.016% (Cr), 0.207% (Mn), 0.062% (Ni), 0.029% (Cu), 0.012% (Mo), <0.001% (V), 0.032% (Si), <0.0005% (P), 0.0059% (S), 0.011% (Co), 0.045% (Al), <0.0010 (Nb), <0.0005% (Ti), <99.3% (Fe).

Coupon B: 0.168% (C), 0.038% (Cr), 0.495% (Mn), 0.034% (Ni), 0.074% (Cu), 0.0081% (Mo), 0.001% (V), 0.237% (Si), 0.014% (P), 0.024% (S), 0.011% (Co), 0.080% (Al), 0.0019 (Nb), 0.0015% (Ti), <98.6% (Fe).

Solutions

Corrosion inhibition tests have been performed in 0.5 M NaCl in the presence of CO₂ (1 atm) at 40° C. as well as at higher pressure (10 bar) of CO₂ and temperature of 120° C. De-aeration of the solution was achieved by purging with 99.999% N₂ (30 min) and then the solution was saturated by continuously bubbling with 99.999% pure CO₂. During polarization measurements, instead of bubbling, the gentle flow of CO₂ was maintained above the surface of the solution without agitating the bulk of the solution. The corrosion caused by oxygen is avoided by the use of the high purity CO₂. In an aqueous solution of CO₂, at pH <4 the corrosion usually occurs by reaction with H⁺, while above pH 4 the active species is adsorbed CO₂ or H₂CO₃ [S. Nesic, K. L. J. Lee, A mechanistic model for carbon dioxide corrosion of mild steel in the presence of protective iron carbonate films-part 3: film growth model, Corrosion, 59 (2003) 616-627. Incorporated herein in its entirety]. In order to avoid any change in the corrosion mechanism, a solution of NaHCO₃ (100 mg/L) was used to maintain the pH between 5.0 and 5.5.

Electrochemical Measurements Tafel Extrapolations

The polarization studies were carried out in a 250 cm³ of 0.5 M NaCl solution at 40° C. in the presence of CO₂ (1 atm), and furthermore, in both the absence and presence of inhibitors at various concentration thereof. The electrochemical cell, assembled in a 750 cm³ round-bottom flask, consisted of a saturated calomel electrode (SCE) as a reference electrode, a mild steel working electrode, and a graphite electrode (≈5 mm diameter) as a counter electrode. The bubbler has one outlet and inlet for the CO₂. The polarization curves were recorded by a computer controlled potentiostat-galvanostat (Auto Lab, Booster 10A-BST707A, Eco Chemie, Netherlands). A computer (Windows 7) loaded with NOVA (Version 1.8) software processed the data. All three electrode cells were connected to the potentiostat (Auto Lab), and used for measurements. A stable open circuit potential was achieved after pre-corroding the working electrode in the solution; within a time frame of 30-60 min. A scan of ±250 mV with respect to the open circuit potential E_(corr) is conducted at a rate of 0.5 mV/s.

Linear Polarization Resistance (LPR) Method

The cell described above was also used for the LPR measurement. The current potential plots (in a range of ±10 mV around E_(corr)) provided the polarization resistance values.

Gravimetric Measurements at High Temperature and Pressure: Autoclave Experiments

The weight-loss measurements at a high temperature of 120° C. and a CO₂ pressure of 10 bar in 0.5 M NaCl solution (250 cm³) in the absence and presence of inhibitors (200 ppm) was carried out in a R&D Autoclave Bolted Closure System (Autoclave Engineers, Model #401C-0679) for 48 h. The detailed experimental procedure is described in our earlier work [M. A. J. Mazumder, H. A. Al-Muallem, M. Faiz, S. A. Ali, Design and synthesis of a novel class of inhibitors for mild steel corrosion in acidic and carbon dioxide-saturated saline media, Corros. Sci. (2014), DOI: 10.1016/j. Incorporated herein by reference in its entirety]. The carbon-steel coupons prepared as described (vide supra) were immersed into the test solution.

Measurement of Surface Tension

The surface tension of the imidazoline samples in 0.5 M NaCl solution at 40° C. were measured by PHYWE surface tensiometer (Germany) following the operating principle of the du Nouy ring method. The surface tensiometer equipped with a torsion dynamometer (0.01 N) and a platinum iridium ring with a diameter of 1.88 cm was used to measure the tear off force. Solutions of different concentrations were prepared from 0.5 M NaCl and equilibrated to 40° C. Solutions of CO₂ saturated 0.5 M NaCl was made by passing CO₂ gas at 40° C.

The standard free energy of micelle formation (ΔG°_(mic))

The ΔG°_(mic) of the synthesized imidazoline surfactant is given by Eq. (6):

ΔG° _(mic)=RTln(C _(corr)/mol L ⁻¹)  (6)

[H.-J. Butt, K. Graf, M. Kappl, Physics and Chemistry of Interfaces. Wiley-VCH, Weinheim, 2003 pp. 253 Incorporated herein in its entirety.] where R, T and C_(corr) represent the gas constant, temperature and concentration of the surfactant at the critical micelle concentration (CMC).

X-Ray Photoelectron Spectroscopy

The metal coupons of dimension 2.5×2.0×0.1 cm³ as treated in the electrochemical tests in CO₂ saturated 0.5 M NaCl at 40° C. for 6 h were rinsed with distilled deionized water and dried under N₂. The XPS analysis using Advantage software for all data processing, was performed using a Thermos Scientific X-ray photoelectron spectrometer (Model #Escalab 250 Xi) and the samples were irradiated with monochromated Al K_(α) X-rays (1486.6 eV) of spot size of diameter 650 μm. The spectra were referenced with a C 1 s peak at 285.4 eV. XPS spectra were deconvoluted using non-linear least squares algorithm with a Shirley base line and a Gaussian-Lorentzian combination.

Synthesis of the Corrosion Inhibitors

As outlined in Scheme 2, p-hydroxybenzoic acid was O-alkylated to give p-alkoxycarboxylic acid in excellent yields. A mixture of an equimolar amount of the acid and DETA was heated at temperatures ranging from 185-250° C. initially using a procedure as described in: Y. Wu, P. R. Herrington, Thermal reactions of fatty acids with diethylene triamine. J. Am. Oil Chem. Soc. 74 (1997) 61-64, and Y. Duda, R. G. Rueda, M. Galicia, H. I. Beltran, L. S. Z. Rivera, Corrosion inhibitors: Design, performance, and computer simulations J. Phys. Chem. B, 109 (2005) 22674-22684, which are incorporated herein by reference in their entirety, in order to generate the imidazolines (VIII). However, a complicated mixture of products that contained variable amounts of the unreacted acid and amide along with the desired imidazoline (VIII) (≈50%) was obtained. This mixture may as well serve as an effective inhibitor mixture. However, one objective was to synthesize and determine the inhibition efficiencies of the pure imidazolines alone. In order to pursue the synthesis of the proposed imidazolines, a different synthetic protocol was designed; the use of nitrile (CN) instead of an acid (CO₂H) group was envisaged. For this purpose, nitriles have been prepared in excellent yields as illustrated in Scheme 2. The reaction of the nitrile with DETA was carried out using the procedure as mentioned in U.S. Pat. No. 4,420,619, [A. Marxer, Imidazole urea and amido compounds. (1983), Incorporated herein by reference in its entirety.] However, the use of CS₂ as a catalyst failed to give the imidazoline (VIII) in the temperature range 110-145° C. A further modification of the catalyst to cysteine HCl, and maintaining a precise temperature range of 140° C. to 150° C., led to the formation of the imidazolines (VIII) and (IX) using DETA (VI) and TEPA (VII), respectively, with excellent yields. In a most preferred embodiment, the reaction temperature is maintained at 145° C. The imidazolines were readily identified by ¹ H and ¹³C NMR spectroscopy. The ¹H NMR spectra of the imidazolines VIIIa and IXa and a ¹³C NMR spectra of VIIIc and IXc are shown in FIGS. 3 and 4, respectively. The carbon spectra revealed the presence of four and eight signals for the carbons marked as a-d and a-h in VIIIc and IXc, respectively.

Preparing a series of imidazolines, bearing different N-substituents and alkoxy chains, allows for the assessment and comparison of their inhibition effects. Two commercial inhibitor samples: QI80-E (R=C₁₂ to C₂₂) from Materials Performance and ARMOHIB 219 from AKZO NOBEL were also tested for the purpose of comparison and are shown below:

Electrochemical Measurements Tafel Extrapolation

The corrosion inhibition results of inhibitors VIIIa-c and IXa-c, carried out in a CO₂-saturated 0.5 M NaCl solution using Tafel plot extrapolation, are summarized in Tables 1 and 2. The pH was kept in the range of 5.0-5.5 to minimize the direct reduction of H₂CO₃ (Eq. 1) [W. Durnie, R. De Marco, A. Jefferson, B. Kinsella, Development of a structure-activity relationship for oil field corrosion inhibitors, J. Electrochem. Soc. 146 (1999) 1751-1756. S. Nesic, G. T. Solvi, J. Enerhaug, Comparison of the rotating cylinder and pipe flow tests for flow-sensitive carbon dioxide corrosion, Corrosion 10 (1995) 51773-787. Incorporated herein by reference in their entirety]. Some representative Tafel plots are shown in FIGS. 5A, 5B, 5C, and 5D. Each pair of Tafel plots was analyzed [S. A. Ali, M. T. Saeed, S. U. Rahman, The isoxazolidines: a new class of corrosion inhibitors of mild steel in acidic medium, Corros. Sci. 45 (2003) 253-266. Incorporated herein by reference in its entirety.] in order to obtain the corrosion current density (i_(corr)) and the corrosion potential (E_(corr)). The extrapolation of cathodic Tafel lines with respect to free corrosion potential from Tafel plots was determined by using a computer (Windows 7) controlled potentiostat-galvanostat (AutoLab, Eco Chemie, Netherlands) instrument with the utilization of an automated linear curve fitting Nova 1.8 software.

LPR

The η% from a LPR technique was calculated using Eq. (7):

$\begin{matrix} {{\eta (\%)} = {\left( \frac{R_{p}^{\prime} - R_{p}}{R_{p}^{\prime}} \right) \times 100}} & (7) \end{matrix}$

where R_(p) and R′_(p) are the respective polarization resistances in solution without or with the inhibitors in CO₂-saturated 0.5 M NaCl at 40° C. (Tables 3 and 4). Tables 3 and 4 also include inhibition data obtained at 30° C. and 50° C. The results of the Tafel extrapolation and LPR at 40° C. are compared in Table 5.

Adsorption Isotherms

Fractional inhibition efficiency η, equated to surface coverage θ of the electrode by an inhibitor molecule at its lower concentration range, is reported in Tables 1-4. Note that at higher inhibitor concentrations, the η versus θ relationship does not remain linear owing to a transition from a monolayer to a multilayer coverage. The θ values obtained by the LPR method (Tables 3 and 4) in CO₂-saturated 0.5 M NaCl, and C (the concentration in mol/L), were used to find the best among the following adsorption isotherms, namely:

Temkin:

=

  (8)

Langmuir: θ/(1−θ)=K _(ads) C  (9)

Frumkin [37]: K _(ads) C={θ/(1−θ)}e ^(−2αθ)  (10)

Freundluich [38]: θ=K_(ads)C^(η)  (11)

where K_(ads) is the equilibrium constant of the adsorption process. The correlation coefficient revealed the best fit for the Langmuir isotherm for the inhibitors in CO₂ saturated 0.5 M NaCl in FIGS. 6A, 6B, 6C, and 6D, and it is also presented in Table 6. Some of the inhibitors demonstrated a good fit for both the Temkin, as well as Langmuir, adsorption isotherms. The molecular interaction parameter f, which describes molecular interactions in the adsorption layer as well as inhomogeneities on the surface of the electrode, was calculated from the Temkin isotherm (Table 6). [W. Durnie, R. De Marco, A. Jefferson, B. Kinsella, Development of a structure-activity relationship for oil field corrosion inhibitors, J. Electrochem. Soc. 146 (1999) 1751-1756. J. O'M. Bockris, S. U. M. Khan, Surface electrochemistry: A molecular level approach, Plenum press, New York and London, 1993, Incorporated herein by reference in their entirety.]

The K_(ads) is related to the free energy of adsorption (ΔG°_(ads)), by:

$\begin{matrix} {K_{ads} = {\frac{1}{55.5}{\exp \left( \frac{{- \Delta}\; G_{ads}}{RT} \right)}}} & (12) \end{matrix}$

The values of and K_(ads) and ΔG°_(ads) are summarized in Table 7. The ΔS°_(ads) and ΔH°_(ads) for the adsorption process of the imidazolines VIIIc and IXc in the temperature range of 30-50° C. was obtained from a plot of ΔG°_(ads) versus T as shown in FIG. 7.

Gravimetric Measurements in CO₂-Saturated 0.5 M NaCl at High Temperature and Pressure

The results of the experiments carried out at temperature of 120° C. and a pressure of 10 bar CO₂ in 0.5 M NaCl for 48 h are given in Table 8. Duplicate determinations were made in each case using coupons of almost identical masses. Percent inhibition efficiency (η%) was calculated using Eq. (13):

$\begin{matrix} {{\eta \mspace{14mu} \%} = {\frac{{{Weight}\mspace{14mu} {loss}\mspace{14mu} ({blank})} - {{Weight}\mspace{14mu} {loss}\mspace{14mu} ({inhibitor})}}{{Weight}\mspace{14mu} {loss}\mspace{14mu} ({blank})} \times 100}} & (13) \end{matrix}$

Where the masses of the coupons differed, relative weight loss of the coupons were used to calculate η% [S. A. Ali, M. T. Saeed, S. U. Rahman, The isoxazolidines: a new class of corrosion inhibitors of mild steel in acidic medium, Corros. Sci. 45 (2003) 253-266.6, S. A. Ali, H. A. Al-Muallem, M. T. Saeed, S. U. Rahman, Hydrophobic-tailed bicycloisoxazolidines: A comparative study of the newly synthesized compounds on the inhibition of mild steel corrosion in hydrochloric and sulfuric acid media, Corros. Sci. 50 (2008) 664-675. Incorporated herein by reference in their entirety]. The average η%, as reported in Table 8, is found to have a standard deviation of 2-3%.

Surface Tension

The surface tension γ and critical CMC values for the imidazolines VIII and IX are measured in 0.5 M NaCl and 0.5 M NaCl+CO₂ at 40° C. and the results are given in Table 9. FIGS. 8A, 8B show the plot of surface tension γ against the concentration of the imidazolines under various conditions.

X-Ray Photoelectron Spectroscopy

The plots of the intensity (counts) versus binding energy (eV) as measured by XPS are shown in FIGS. 9A, 9B, 9C, 9D, 9E, 9F and 10A, 10B, 10C. The results of the surface analysis are given in Table 10.

Thus, the foregoing discussion discloses and describes merely exemplary embodiments of the present invention. As will be understood by those skilled in the art, the present invention may be embodied in other specific forms without departing from the spirit or essential characteristics thereof. Accordingly, the disclosure of the present invention is intended to be illustrative, but not limiting of the scope of the invention, as well as other claims. The disclosure, including any readily discernible variants of the teachings herein, defines, in part, the scope of the foregoing claim terminology such that no inventive subject matter is dedicated to the public. 

1. A composition comprising an aminoalkyl imidazoline of formula (I)

wherein m is an integer of 2 to 4; R is a C₂ alkylene; R₁ is an aromatic hydrocarbon of formula (II)

wherein X is oxygen; R′₁ to R′₄ are each independently selected from the group consisting of hydrogen, C₁-C₃₀ alkyl, aminoalkyl, and aminoaryl; R′₅ is a C₅-C₃₀ alkyl group; and R₂ and R₃ and are each independently selected from the group consisting of hydrogen, hydroxyl, halogen, C₁-C₃₀ alkyl, alkenyl, aryl, alkylaryl, arylalkyl, aminoalkyl, aminoaryl, (CH₂)₂COOH, CH₂CH(CH₃)COOH, and imidazoline.
 2. The composition of claim 1 wherein the aminoalkyl imidazoline comprises a 2-imidazoline ring substituted with an ethanamine group at a 5-N position of the 2-imidazoline ring, and a p-octyloxy phenyl group at a 1-C position of the 2-imidazoline ring.
 3. The composition of claim 1 wherein the aminoalkyl imidazoline comprises a 2-imidazoline ring substituted with an ethanamine group at a 5-N position of the 2-imidazoline ring, and a p-dodecyloxy phenyl group at a 1-C position of the 2-imidazoline ring.
 4. The composition of claim 1 wherein the aminoalkyl imidazoline comprises a 2-imidazoline ring substituted with an ethanamine group at a 5-N position of the 2-imidazoline ring, and a p-octadecyloxy phenyl group at the 1-C position of the 2-imidazoline ring.
 5. The composition of claim 1 wherein the aminoalkyl imidazoline comprises a 2-imidazoline ring substituted with a N¹-(2-aminoethyl)-N²-ethylethane-1,2-diamine group at a 5-N position of the 2-imidazoline ring, and a p-octyloxy phenyl group at a 1-C position of the 2-imidazoline ring.
 6. The composition of claim 1 wherein the aminoalkyl imidazoline comprises a 2-imidazoline ring substituted with a N¹-(2-aminoethyl)-N²-ethylethane-1,2-diamine group at a 5-N position of the 2-imidazoline ring, and a p-dodecyloxy phenyl group at a 1-C position of the 2-imidazoline ring.
 7. The composition of claim 1 wherein the aminoalkyl imidazoline comprises a 2-imidazoline ring substituted with a N¹-(2-aminoethyl)-N²-ethylethane-1,2-diamine group at a 5-N position of the 2-imidazoline ring, and a p-octadecyloxy phenyl group at the 1-C position. 8-13. (canceled)
 14. The composition of claim 1 further comprising one or more additives selected from the group consisting of surfactants, intensifiers, solvents, oil-wetting components, dispersants, scale inhibitors and biocides.
 15. A method of preventing or reducing corrosion, comprising: adding to a process stream an effective corrosion inhibiting amount of one or more aminoalkyl imidazolines of formula (I)

wherein m is an integer of 2 to 4; R is a C₂ alkylene; R₁ is an aromatic hydrocarbon of formula (II)

wherein X is oxygen; R′₁ to R′₄ are each independently selected from the group consisting of hydrogen C₁-C₃₀ alkyl, aminoalkyl, and aminoaryl; R′₅ is a C₅-C₃₀ alkyl group; and R₂ and R₃ and are each independently selected from the group consisting of hydrogen, hydroxyl, halogen, C₁-C₃₀ alkyl, alkenyl, aryl, alkylaryl, arylalkyl, aminoalkyl, aminoaryl, (CH₂)₂COOH, CH₂CH(CH₃)COOH, and imidazoline.
 16. The method of claim 15 wherein the process stream comprises at least one constituent selected from the group consisting of water, petroleum, and petroleum products, and at least one constituent selected from the group consisting of carbon dioxide (CO₂), hydrogen sulfide (H₂S), and NaCl.
 17. The method of claim 15 wherein said effective corrosion inhibiting amount is 0.1 to 1,000 ppm by weight of the aminoalkyl imidazoline.
 18. The method of claim 15 wherein said effective corrosion inhibiting amount is 1.0 to 500 ppm by weight of the aminoalkyl imidazoline.
 19. The method of claim 15 wherein said adding of the aminoalkyl imidazolines is continuous or intermittent.
 20. A method of inhibiting a metal corrosive process of a mild steel surface in contact with a process stream comprising at least one constituent selected from the group consisting of water, petroleum, and petroleum products, the method comprising: contacting the mild steel surface with the composition of claim 1 by spraying the mild steel surface with the composition, dipping the mild steel surface into the composition, and/or adding the composition to said process stream and contacting said mild steel surface with the process stream. 